Non-coordinating anion type activators containing cation having aryldiamine groups and uses thereof

ABSTRACT

The present disclosure provides borate or aluminate activators comprising cations having linear alkyl groups, catalyst systems comprising, and methods for polymerizing olefins using such activators.

CROSS REFERENCE TO RELATED APPLICATIONS

This application claims the priority benefit of U.S. Provisional Application No. 62/948,692, filed Dec. 16, 2019, the disclosure of which is incorporated herein by reference.

This disclosure relates to: U.S. Ser. No. 16/394,166, filed Apr. 25, 2019, U.S. Ser. No. 16/394,197, filed Apr. 25, 2019, and U.S. Ser. No. 62/882,088 filed Aug. 2, 2019.

FIELD

The present disclosure provides group 13 metallate activators, catalyst systems comprising group 13 metallate activators, and methods for polymerizing olefins using such activators.

BACKGROUND

Polyolefins are widely used commercially because of their robust physical properties. Polyolefins are typically prepared with a catalyst that polymerizes olefin monomers. Therefore, there is interest in finding new catalysts and catalyst systems that provide polymers having improved properties.

Catalysts for olefin polymerization are often based on metallocenes as catalyst precursors, which are activated either with an alumoxane or an activator containing a non-coordinating anion. A non-coordinating anion, such as tetrakis(pentafluorophenyl)borate, is capable of stabilizing the resulting metal cation of the catalyst. Because such activators are fully ionized and the corresponding anion is highly non-coordinating, such activators can be effective as olefin polymerization catalyst activators. However, because they are ionic salts, such activators are insoluble in aliphatic hydrocarbons and only sparingly soluble in aromatic hydrocarbons. It may be advantageous to conduct polymerizations of α-olefins in aliphatic hydrocarbon solvents due to the compatibility of such solvents with the olefin monomer and in order to reduce the aromatic hydrocarbon content of the resulting polymer product. Typically, ionic salt activators are added to such polymerizations in the form of a solution in an aromatic solvent such as toluene. The use of even a small quantity of such an aromatic solvent to dissolve the activator may be undesirable since the aromatics must be removed in a post-polymerization devolatilization step and separated from other volatile components, which is a process that adds significant cost and complexity to commercial processes. In addition, the activators often exist in the form of an oily, intractable material which is not readily handled and metered or precisely incorporated into the reaction mixture.

U.S. Pat. No. 5,919,983 discloses polymerization of ethylene and octene using a catalyst system including [(C₁₈)₂MeNH)]⁺[B(PhF₅)₄]⁻ activator having four fluoro-phenyl groups bound to the boron atom and two linear C₁₈ groups bound to the nitrogen, as well as describing other linear groups at column 3, line 51 et seq.

U.S. Pat. No. 8,642,497 discloses the preparation of N,N-dimethylanilinium tetrakis(heptafluoronaphth-2-yl)borate anion.

US 2003/0013913 (granted as U.S. Pat. No. 7,101,940) discloses various activators such as N,N-dimethylcyclohexylammoniumtetrakis(pentafluorophenyl)borate [0070], and N,N-diethylbenzylammoniumtetrakis(pentafluorophenyl)borate [0124].

US 2002/0062011 discloses phenyldioctadecylammonium (hydroxyphenyl) tris(pentafluorophenyl) borate at paragraph [0200] and (pentafluorophenyl) dioctadecylammonium tetrakis(pentafluorophenyl) borate at paragraph [0209].

U.S. Pat. Nos. 7,799,879; 7,985,816; 8,580,902; 8,835,587 and WO 2010/014344 describe ammonium borate activators that include some that use a tetrakis(heptafluoronaphth-2-yl)borate anion.

There is a need for activators that are soluble in aliphatic hydrocarbons and capable of producing polyolefins having high molecular weight and high melt temperature. Likewise, there is a need for activators that are soluble in aliphatic hydrocarbons and capable of producing polyolefins at high activity levels where the polymers may have high molecular weights, high melt temperatures, and reduced or eliminated aromatic content.

References of interest include: WO 2002/002577; U.S. Pat. Nos. 7,087,602; 8,642,497; 6,121,185; 8,642,497; 8,519,037; US 2015/0203602; and U.S. Ser. No. 62/662,972 filed Apr. 26, 2018, CAS Number 1225373-54-5 (N¹,N¹,N⁵,N⁵-tetrabutyl-1,5-naphthalenylenediamine); CAS Number 1159250-18-6 (N¹,N¹,N⁵,N⁵-tetraoctyl-1,5-naphthalenylenediamine); U.S. Ser. No. 16/394,174, filed Apr. 25, 2019; U.S. Ser. No. 16/394,186, filed Apr. 25, 2019; U.S. Ser. No. 16/394,197, filed Apr. 25, 2019; U.S. Ser. No. 16/394,520, filed Apr. 25, 2019; and U.S. Ser. No. 16/394,566, filed Apr. 25, 2019; U.S. Ser. No. 16/394,166, filed Apr. 25, 2019; and U.S. Ser. No. 62/882,088 filed Aug. 2, 2019.

Englund, V. et al. (2009) “High Efficiency Voltage Stabalizers for XLPE Cable Insulation,” Polymer Degredation and Stability, v.94(5), pp. 823-833.

SUMMARY

The present disclosure is related to activator compounds represented by Formula (I): [Ar(E¹R¹R²H)_(x)(E²R³R⁴)_(y)][QR⁵R⁶R⁷R⁸]_(z)  (I) In Formula (I) each of E¹ and E² are nitrogen and Ar is a C₁₀-C₃₀ multicyclic aromatic hydrocarbyl group, where E¹ is a first Ar substitution located on a first ring of the multicyclic aromatic hydrocarbyl group and E² is a second Ar substitution located on a second ring of the multicyclic aromatic hydrocarbyl group. In addition, in Formula (I) x is 1 to 4; y is 0 to 3; z=x; and x+y is 2 to 6; Q is an element selected from group 13 of the Periodic Table of the Elements. Additionally, each of R¹, R², R³, and R⁴ are independently selected from C₁-C₄₀ aliphatic hydrocarbyl, substituted C₁-C₄₀ aliphatic hydrocarbyl, wherein R¹, R², R³, and R⁴ together include 15 or more carbon atoms and each of R⁵, R⁶, R⁷, and R⁸ is independently a hydride, bridged or unbridged dialkylamido, halide, alkoxide, aryloxide, hydrocarbyl, substituted hydrocarbyl, halocarbyl, or substituted halocarbyl.

In yet another embodiment, the present disclosure provides a catalyst system including an activator as described herein and a catalyst compound.

In still another embodiment, the present disclosure provides a polymerization process including a) contacting one or more olefin monomers with a catalyst system including: an activator as described herein and a catalyst compound.

In still another embodiment, the present disclosure provides a polyolefin formed by a catalyst system and or method of the present disclosure.

BRIEF DESCRIPTION OF THE FIGURES

FIG. 1 is a graph depicting ethylene polymerization activity with catalyst systems including activators of the present disclosure, according to some embodiments.

FIG. 2 is a graph depicting propylene polymerization activity with catalyst systems including activators of the present disclosure, according to some embodiments.

FIG. 3 is a graph depicting ethylene:octene polymerization activity with catalyst systems including activators of the present disclosure, according to some embodiments.

DETAILED DESCRIPTION

The present disclosure relates to activator compounds that can be used in olefin polymerization processes. For example, the present disclosure provides activators, catalyst systems including catalyst compounds and activators, and methods for polymerizing olefins using said catalyst systems. In the present disclosure, activators are described that feature ammonium groups with aliphatic hydrocarbyl groups for improved solubility of the activator in aliphatic solvents, as compared to conventional activator compounds.

The present disclosure relates to activator compounds that can be used in olefin polymerization processes. For example, the present disclosure provides ammonium cations coupled with non-coordinating anions of group 13, such as sterically hindered borates and aluminates. Also provided are catalyst systems including such activators and methods for polymerizing olefins using the activators. In the present disclosure, activators are described that feature ammonium groups with aliphatic hydrocarbyl groups for improved solubility of the activator in aliphatic solvents, as compared to conventional activator compounds. Useful non-coordinating anions of the present disclosure include perfluoronaphthalenyl or perfluorophenyl borates or aluminates. It has been discovered that activators of the present disclosure having perfluoronaphthalenyl borate or aluminate anions have improved solubility in aliphatic solvents, as compared to conventional activator compounds. Activators of the present disclosure can provide polyolefin homopolymers having a weight average molecular weight (Mw) of about 300,000 g/mol or greater and a melt temperature (Tm) of about 130° C. or greater. Further, activators having a cation having two or more C₆ to C₃₀ alkyl groups can provide enhanced activity for polymer production.

Definitions

Unless otherwise noted all melt temperatures (Tm) are DSC second melt and are determined using the following DSC procedure according to ASTM D3418-03. Differential scanning calorimetric (DSC) data are obtained using a TA Instruments model Q200 machine. Samples weighing about 5 to about 10 mg are sealed in an aluminum hermetic sample pan. The DSC data are recorded by first gradually heating the sample to about 200° C. at a rate of about 10° C./minute. The sample is kept at about 200° C. for about 2 minutes, then cooled to about −90° C. at a rate of about 10°/minute, followed by an isothermal for about 2 minutes and heating to about 200° C. at about 10° C./minute. Both the first and second cycle thermal events are recorded. The melting points reported are obtained during the second heating/cooling cycle unless otherwise noted.

All molecular weights are weight average (Mw) unless otherwise noted. All molecular weights are reported in g/mol unless otherwise noted. Melt index (MI) also referred to as 12, reported in g/10 min, is determined according to ASTM D-1238, 190° C., 2.16 kg load. High load melt index (HLMI) also referred to as 121, reported in g/10 min, is determined according to ASTM D-1238, 190° C., 21.6 kg load. Melt index ratio (MIR) is MI divided by HLMI as determined by ASTM D1238.

The specification describes catalysts that can be transition metal complexes. The term complex is used to describe molecules in which an ancillary ligand is coordinated to a central transition metal atom. The ligand is bulky and stably bonded to the transition metal to maintain its influence during use of the catalyst, such as polymerization. The ligand may be coordinated to the transition metal by covalent bond and/or electron donation coordination or intermediate bonds. The transition metal complexes are typically subjected to activation to perform their polymerization or oligomerization function using an activator, which is believed to create a cation as a result of the removal of an anionic group, often referred to as a leaving group, from the transition metal.

For the purposes of the present disclosure, the numbering scheme for the Periodic Table Groups is the “New” notation as described in Chemical and Engineering News, v.63(5), pg. 27 (1985). Therefore, a “Group 8 metal” is an element from Group 8 of the Periodic Table, e.g., Fe, and so on.

The following abbreviations are used throughout this disclosure: o-biphenyl is an ortho-biphenyl moiety represented by the structure

dme is 1,2-dimethoxyethane, Me is methyl, Ph is phenyl, Et is ethyl, Pr is propyl, iPr is isopropyl, n-Pr is normal propyl, cPr is cyclopropyl, Bu is butyl, iBu is isobutyl, tBu is tertiary butyl, p-tBu is para-tertiary butyl, nBu is normal butyl, sBu is sec-butyl, TMS is trimethylsilyl, TIBAL is triisobutylaluminum, TNOAL is tri(n-octyl)aluminum, MAO is methylalumoxane, p-Me is para-methyl, Ph is phenyl, Bn is benzyl (i.e., CH₂Ph), THF (also referred to as the is tetrahydrofuran, RT is room temperature (and is 23° C. unless otherwise indicated), tol is toluene, EtOAc is ethyl acetate, MeCy is methylcyclohexane, and Cy is cyclohexyl.

Unless otherwise indicated (e.g., the definition of “substituted hydrocarbyl”, etc.), the term “substituted” means that at least one hydrogen atom has been replaced with at least a non-hydrogen group, such as a hydrocarbyl group, a heteroatom, or a heteroatom containing group, such as halogen (such as Br, Cl, F or I) or at least one functional group such as —NR*₂, —OR*, —SeR*, —TeR*, —PR*₂, —AsR*₂, —SbR*₂, —SR*, —BR*₂, —SiR*, —SiR*₃, —GeR*, —GeR*₃, —SnR*, —SnR*₃, —PbR*₃, and the like, where each R* is independently a hydrocarbyl or halocarbyl radical, and two or more R* may join together to form a substituted or unsubstituted saturated, partially unsaturated or aromatic cyclic or polycyclic ring structure, or where at least one heteroatom has been inserted within a ring structure.

The terms “hydrocarbyl radical,” “hydrocarbyl,” and “hydrocarbyl group,” are used interchangeably throughout this disclosure. Likewise, the terms “group”, “radical”, and “substituent” are also used interchangeably in this disclosure. For purposes of this disclosure, “hydrocarbyl radical” is defined to be C₁-C₁₀₀ radicals of carbon and hydrogen, that may be linear, branched, or cyclic, and when cyclic, aromatic or non-aromatic. Examples of such radicals can include methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, tert-butyl, pentyl, iso-amyl, hexyl, octyl cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cyclooctyl, and the like.

Substituted hydrocarbyl radicals are radicals in which at least one hydrogen atom of the hydrocarbyl radical has been replaced with a heteroatom, or a heteroatom containing group, such as halogen (such as Br, Cl, F or I) or at least one functional group such as —NR*₂, —OR*, —SeR*, —TeR*, —PR*₂, —AsR*₂, —SbR*₂, —SR*, —BR*₂, —SiR*, —SiR*₃, —GeR*, —GeR*₃, —SnR*, —SnR*₃, —PbR*₃, and the like, where each R* is independently a hydrocarbyl or halocarbyl radical, and two or more R* may join together to form a substituted or unsubstituted saturated, partially unsaturated or aromatic cyclic or polycyclic ring structure, or where at least one heteroatom has been inserted within a hydrocarbyl ring.

Substituted cyclopentadienyl, indenyl, tetrahydroindenyl or fluorenyl groups are cyclopentadienyl, indenyl, tetrahydroindenyl or fluorenyl groups where at least one hydrogen atom has been replaced with at least a non-hydrogen group, such as a hydrocarbyl group, a heteroatom, or a heteroatom containing group, such as halogen (such as Br, Cl, F or I) or at least one functional group such as —NR*₂, —OR*, —SeR*, —TeR*, —PR*₂, —AsR*₂, —SbR*₂, —SR*, —BR*₂, —SiR*, —SiR*₃, —GeR*, —GeR*₃, —SnR*, —SnR*₃, —PbR*₃, and the like, where each R* is independently a hydrocarbyl or halocarbyl radical, and two or more R* may join together to form a substituted or unsubstituted saturated, partially unsaturated or aromatic cyclic or polycyclic ring structure, or where at least one heteroatom has been inserted within a ring structure.

Halocarbyl radicals (also referred to as halocarbyls, halocarbyl groups or halocarbyl substituents) are radicals in which one or more hydrocarbyl hydrogen atoms have been substituted with at least one halogen (e.g., F, Cl, Br, I) or halogen-containing group (e.g., CF₃). Substituted halocarbyl radicals are radicals in which at least one halocarbyl hydrogen or halogen atom has been substituted with at least one functional group such as NR*₂, OR*, SeR*, TeR*, PR*₂, AsR*₂, SbR*₂, SR*, BR*₂, SiR*₃, GeR*₃, SnR*₃, PbR*₃, and the like or where at least one non-carbon atom or group has been inserted within the halocarbyl radical such as —O—, —S—, —Se—, —Te—, —N(R*)—, ═N—, —P(R*)—, ═P—, —As(R*)—, ═As—, —Sb(R*)—, ═Sb—, —B(R*)—, ═B—, —Si(R*)₂—, —Ge(R*)₂—, —Sn(R*)₂—, —Pb(R*)₂— and the like, where R* is independently a hydrocarbyl or halocarbyl radical provided that at least one halogen atom remains on the original halocarbyl radical. Additionally, two or more R* may join together to form a substituted or unsubstituted saturated, partially unsaturated or aromatic cyclic or polycyclic ring structure.

Hydrocarbylsilyl groups, also referred to as silylcarbyl groups, are radicals in which one or more hydrocarbyl hydrogen atoms have been substituted with at least one SiR*₃ containing group or where at least one —Si(R*)₂— has been inserted within the hydrocarbyl radical where R* is independently a hydrocarbyl or halocarbyl radical, and two or more R* may join together to form a substituted or unsubstituted saturated, partially unsaturated or aromatic cyclic or polycyclic ring structure. Silylcarbyl radicals can be bonded via a silicon atom or a carbon atom.

Substituted silylcarbyl radicals are silylcarbyl radicals in which at least one hydrogen atom has been substituted with at least one functional group such as NR*₂, OR*, SeR*, TeR*, PR*₂, AsR*₂, SbR*₂, SR*, BR*₂, GeR*₃, SnR*₃, PbR₃ and the like or where at least one non-hydrocarbon atom or group has been inserted within the silylcarbyl radical, such as —O—, —S—, —Se—, —Te—, —N(R*)—, ═N—, —P(R*)—, ═P—, —As(R*)—, ═As—, —Sb(R*)—, ═Sb—, —B(R*)—, ═B—, —Ge(R*)₂—, —Sn(R*)₂—, —Pb(R*)₂— and the like, where R* is independently a hydrocarbyl or halocarbyl radical, and two or more R* may join together to form a substituted or unsubstituted saturated, partially unsaturated or aromatic cyclic or polycyclic ring structure.

Germylcarbyl radicals (also referred to as germylcarbyls, germylcarbyl groups or germylcarbyl substituents) are radicals in which one or more hydrocarbyl hydrogen atoms have been substituted with at least one GeR*₃ containing group or where at least one —Ge(R*)₂— has been inserted within the hydrocarbyl radical where R* is independently a hydrocarbyl or halocarbyl radical, and two or more R* may join together to form a substituted or unsubstituted saturated, partially unsaturated or aromatic cyclic or polycyclic ring structure. Germylcarbyl radicals can be bonded via a germanium atom or a carbon atom.

Substituted germylcarbyl radicals are germylcarbyl radicals in which at least one hydrogen atom has been substituted with at least one functional group such as NR*₂, OR*, SeR*, TeR*, PR*₂, AsR*₂, SbR*₂, SR*, BR*₂, SiR*₃, SnR*₃, PbR₃ and the like or where at least one non-hydrocarbon atom or group has been inserted within the germylcarbyl radical, such as —O—, —S—, —Se—, —Te—, —N(R*)—, ═N—, —P(R*)—, ═P—, —As(R*)—, ═As—, —Sb(R*)—, ═Sb—, —B(R*)—, ═B—, —Si(R*)₂—, —Sn(R*)₂—, —Pb(R*)₂— and the like, where R* is independently a hydrocarbyl or halocarbyl radical, and two or more R* may join together to form a substituted or unsubstituted saturated, partially unsaturated or aromatic cyclic or polycyclic ring structure.

The terms “alkyl radical,” and “alkyl” are used interchangeably throughout this disclosure. For purposes of this disclosure, “alkyl radicals” are defined to be C₁-C₁₀₀ alkyls that may be linear, branched, or cyclic. Examples of such radicals can include methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, tert-butyl, pentyl, iso-amyl, hexyl, octyl cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cyclooctyl, and the like. Substituted alkyl radicals are radicals in which at least one hydrogen atom of the alkyl radical has been substituted with at least a non-hydrogen group, such as a hydrocarbyl group, a heteroatom, or a heteroatom containing group, such as halogen (such as Br, Cl, F or I) or at least one functional group such as —NR*₂, —OR*, —SeR*, —TeR*, —PR*₂, —AsR*₂, —SbR*₂, —SR*, —BR*₂, —SiR*, —SiR*₃, —GeR*, —GeR*₃, —SnR*, —SnR*₃, —PbR*₃, and the like, where each R* is independently a hydrocarbyl or halocarbyl radical, and two or more R* may join together to form a substituted or unsubstituted saturated, partially unsaturated or aromatic cyclic or polycyclic ring structure, or where at least one heteroatom has been inserted within a hydrocarbyl ring.

The term “branched alkyl” means that the alkyl group contains a tertiary or quaternary carbon (a tertiary carbon is a carbon atom bound to three other carbon atoms. A quaternary carbon is a carbon atom bound to four other carbon atoms). For example, 3,5,5 trimethylhexylphenyl is an alkyl group (hexyl) having three methyl branches (hence, one tertiary and one quaternary carbon) and thus is a branched alkyl bound to a phenyl group. Unless otherwise indicated a branched alkyl includes all isomers thereof.

The term “alkenyl” means a straight-chain, branched-chain, or cyclic hydrocarbon radical having one or more carbon-carbon double bonds. These alkenyl radicals may be substituted. Examples of suitable alkenyl radicals can include ethenyl, propenyl, allyl, 1,4-butadienyl cyclopropenyl, cyclobutenyl, cyclopentenyl, cyclohexenyl, cyclooctenyl and the like.

The term “arylalkenyl” means an aryl group where a hydrogen has been replaced with an alkenyl or substituted alkenyl group. For example, styryl indenyl is an indene substituted with an arylalkenyl group (a styrene group).

The term “alkoxy”, “alkoxyl”, or “alkoxide” means an alkyl ether or aryl ether radical where the terms “alkyl” and “aryl” are as defined herein. Examples of suitable alkyl ether radicals can include methoxy, ethoxy, n-propoxy, iso-propoxy, n-butoxy, iso-butoxy, sec-butoxy, tert-butoxy, phenoxy, and the like.

The term “aryloxy” or “aryloxide” means an aryl ether radical where the term aryl is as defined herein.

The term “aryl” or “aryl group” means a carbon-containing aromatic ring such as phenyl. Likewise, heteroaryl means an aryl group where a ring carbon atom (or two or three ring carbon atoms) has been replaced with a heteroatom, such as N, O, or S. As used herein, the term “aromatic” also refers to pseudoaromatic heterocycles, which are heterocyclic substituents that have similar properties and structures (nearly planar) to aromatic heterocyclic ligands, but are not by definition aromatic.

Heterocyclic means a cyclic group where a ring carbon atom (or two or three ring carbon atoms) has been replaced with a heteroatom, such as N, O, or S. A heterocyclic ring is a ring having a heteroatom in the ring structure as opposed to a heteroatom substituted ring where a hydrogen on a ring atom is replaced with a heteroatom. For example, tetrahydrofuran is a heterocyclic ring and 4-N,N-dimethylamino-phenyl is a heteroatom substituted ring.

Substituted heterocyclic means a heterocyclic group where at least one hydrogen atom of the heterocyclic radical has been substituted with at least a non-hydrogen group, such as a hydrocarbyl group, a heteroatom, or a heteroatom containing group, such as halogen (such as Br, Cl, F or I) or at least one functional group such as —NR*₂, —OR*, —SeR*, —TeR*, —PR*₂, —AsR*₂, —SbR*₂, —SR*, —BR*₂, —SiR*, —SiR*₃, —GeR*, —GeR*₃, —SnR*, —SnR*₃, —PbR*₃, and the like, where each R* is independently a hydrocarbyl or halocarbyl radical.

A substituted aryl is an aryl group where at least one hydrogen atom of the aryl radical has been substituted with at least a non-hydrogen group, such as a hydrocarbyl group, a heteroatom, or a heteroatom containing group, such as halogen (such as Br, Cl, F or I) or at least one functional group such as —NR*₂, —OR*, —SeR*, —TeR*, —PR*₂, —AsR*₂, —SbR*₂, —SR*, —BR*₂, —SiR*, —SiR*₃, —GeR*, —GeR*₃, —SnR*, —SnR*₃, —PbR*₃, and the like, where each R* is independently a hydrocarbyl or halocarbyl radical, and two or more R* may join together to form a substituted or unsubstituted saturated, partially unsaturated or aromatic cyclic or polycyclic ring structure, or where at least one heteroatom has been inserted within a hydrocarbyl ring, for example 3,5-dimethylphenyl is a substituted phenyl group.

The term “substituted phenyl,” or “substituted phenyl group” means a phenyl group having one or more hydrogen groups replaced by a hydrocarbyl, substituted hydrocarbyl, heteroatom or heteroatom containing group, such as halogen (such as Br, Cl, F or I) or at least one functional group such as —NR*₂, —OR*, —SeR*, —TeR*, —PR*₂, —AsR*₂, —SbR*₂, —SR*, —BR*₂, —SiR*, —SiR*₃, —GeR*, —GeR*₃, —SnR*, —SnR*₃, —PbR*₃, and the like, where each R* is independently a hydrocarbyl, halogen, or halocarbyl radical. The “substituted phenyl” group may be represented by the formula:

where each of R¹⁷, R¹⁸, R¹⁹, R²⁰, and R²¹ is independently selected from hydrogen, C₁-C₄₀ hydrocarbyl or C₁-C₄₀ substituted hydrocarbyl, a heteroatom, such as halogen, or a heteroatom-containing group (provided that at least one of R¹⁷, R¹⁸, R¹⁹, R²⁰, and R²¹ is not H), or a combination thereof.

A “fluorophenyl” or “fluorophenyl group” is a phenyl group substituted with one, two, three, four or five fluorine atoms.

A “fluoroaryl” or “fluoroaryl group” is an aryl group substituted with at least one fluorine atom, such as perfluorinated aryl.

The term “arylalkyl” means an aryl group where a hydrogen has been replaced with an alkyl or substituted alkyl group. For example, 3,5′-di-tert-butyl-phenyl indenyl is an indene substituted with an arylalkyl group. When an arylalkyl group is a substituent on another group, the alkylaryl is bound to that group via the aryl. For example in Formula AI, the aryl portion is bound to E.

The term “alkylaryl” means an alkyl group where a hydrogen has been replaced with an aryl or substituted aryl group. For example, phenethyl indenyl is an indene substituted with an ethyl group bound to a benzene group. When an alkylaryl group is a substituent on another group, the alkylaryl is bound to that group via the alkyl. For example in Formula AI, the alkyl portion is bound to E.

Reference to an alkyl, alkenyl, alkoxide, or aryl group without specifying a particular isomer (e.g., butyl) expressly discloses all isomers (e.g., n-butyl, iso-butyl, sec-butyl, and tert-butyl), unless otherwise indicated.

The term “ring atom” means an atom that is part of a cyclic ring structure. Accordingly, a benzyl group has six ring atoms and tetrahydrofuran has 5 ring atoms.

For purposes of the present disclosure, a “catalyst system” is a combination of at least one catalyst compound, an activator, and an optional support material. The catalyst systems may further include one or more additional catalyst compounds. For the purposes of the present disclosure, when catalyst systems are described as including neutral stable forms of the components, the ionic form of the component is the form that reacts with the monomers to produce polymers. Catalysts of the presented disclosure and activators represented by Formula (I) are intended to embrace ionic forms in addition to the neutral forms of the compounds.

“Complex” as used herein, is also often referred to as catalyst precursor, precatalyst, catalyst, catalyst compound, transition metal compound, or transition metal complex. These words are used interchangeably.

A scavenger is a compound that is typically added to facilitate polymerization by scavenging impurities. Some scavengers may also act as activators and may be referred to as co-activators. A co-activator, that is not a scavenger, may also be used in conjunction with an activator in order to form an active catalyst. In some embodiments, a co-activator can be pre-mixed with the transition metal compound to form an alkylated transition metal compound.

A catalyst may be described as a catalyst precursor, a pre-catalyst compound, a catalyst compound or a transition metal compound, and these terms are used interchangeably. A polymerization catalyst system is a catalyst system that can polymerize monomers into polymer. An “anionic ligand” is a negatively charged ligand, which donates one or more pairs of electrons to a metal ion. A “neutral donor ligand” is a neutrally charged ligand, which donates one or more pairs of electrons to a metal ion.

A metallocene catalyst is defined as an organometallic compound with at least one π-bound cyclopentadienyl moiety or substituted cyclopentadienyl moiety (such as substituted or unsubstituted Cp, Ind, or Flu) and more frequently two (or three) π-bound cyclopentadienyl moieties or substituted cyclopentadienyl moieties (such as substituted or unsubstituted Cp, Ind, or Flu). (Cp=cyclopentadienyl, Ind=indenyl, Flu=fluorenyl).

For purposes of the present disclosure, in relation to catalyst compounds, the term “substituted” means that a hydrogen group has been replaced with a hydrocarbyl group, a heteroatom, or a heteroatom-containing group. For example, methyl cyclopentadiene (Cp) is a Cp group substituted with a methyl group.

“Catalyst productivity” is a measure of how many grams of polymer (P) are produced using a polymerization catalyst including W g of catalyst (cat), over a period of time of T hours; and may be expressed by the following formula: P/(T×W) and expressed in units of gPgcat⁻¹ hr⁻¹. “Conversion” is the amount of monomer that is converted to polymer product, and is reported as mol % and is calculated based on the polymer yield and the amount of monomer fed into the reactor. “Catalyst activity” is a measure of the level of activity of the catalyst and is reported as the mass of product polymer (P) produced per mole (or mmol) of catalyst (cat) used (kgP/molcat or gP/mmolCat), and catalyst activity can be expressed per unit of time, for example, per hour (hr), e.g., (Kg/mmol h).

An “olefin,” alternatively referred to as “alkene,” is a linear, branched, or cyclic compound including carbon and hydrogen having at least one double bond. For purposes of this disclosure, when a polymer or copolymer is referred to as including an olefin, the olefin present in such polymer or copolymer is the polymerized form of the olefin. For example, when a copolymer is said to have a “propylene” content of 35 wt % to 55 wt %, the mer unit in the copolymer is derived from propylene in the polymerization reaction and the derived units are present at 35 wt % to 55 wt %, based upon the weight of the copolymer.

A “polymer” has two or more of the same or different monomer (“mer”) units. A “homopolymer” is a polymer having mer units that are the same. A “copolymer” is a polymer having two or more mer units that are different from each other. A “terpolymer” is a polymer having three mer units that are different from each other. “Different” in reference to mer units indicates that the mer units differ from each other by at least one atom or are different isomerically. Accordingly, copolymer, can include terpolymers and the like. An oligomer is typically a polymer having a low molecular weight, such an Mn of less than 25,000 g/mol, or less than 2,500 g/mol, or a low number of mer units, such as 75 mer units or less or 50 mer units or less. An “ethylene polymer” or “ethylene copolymer” is a polymer or copolymer including at least 50 mol % ethylene derived units, a “propylene polymer” or “propylene copolymer” is a polymer or copolymer including at least 50 mol % propylene derived units, and so on.

Mn is number average molecular weight, Mw is weight average molecular weight, and Mz is z average molecular weight, wt % is weight percent, and mol % is mole percent. Molecular weight distribution (MWD), also referred to as polydispersity index (PDI), is defined to be Mw divided by Mn.

The term “continuous” means a system that operates without interruption or cessation for a period of time, such as where reactants are continually fed into a reaction zone and products are continually or regularly withdrawn without stopping the reaction in the reaction zone. For example, a continuous process to produce a polymer would be one where the reactants are continually introduced into one or more reactors and polymer product is continually withdrawn.

A “solution polymerization” means a polymerization process in which the polymerization is conducted in a liquid polymerization medium, such as an inert solvent or monomer(s) or their blends. A solution polymerization is typically homogeneous. A homogeneous polymerization is one where the polymer product is dissolved in the polymerization medium. Such systems are typically not turbid as described in Oliveira, J. V. et al. (2000) “High-Pressure Phase Equilibria for Polypropylene-Hydrocarbon Systems,” Ind. Eng. Chem. Res., v.39, pp. 4627-4633.

A bulk polymerization means a polymerization process in which the monomers and/or comonomers being polymerized are used as a solvent or diluent using little or no inert solvent or diluent. A small fraction of inert solvent might be used as a carrier for catalyst and scavenger. A bulk polymerization system contains less than about 25 wt % of inert solvent or diluent, such as less than about 10 wt %, such as less than about 1 wt %, such as 0 wt %.

Description

The present disclosure relates to activator compounds that can be used in olefin polymerization processes. For example, the present disclosure provides activators, catalyst systems including catalyst compounds and activators, and methods for polymerizing olefins using said catalyst systems. In the present disclosure, activators are described that feature ammonium groups with long-chain aliphatic hydrocarbyl groups for improved solubility of the activator in aliphatic solvents, as compared to conventional activator compounds.

The present disclosure also relates to polymer compositions obtained from the catalyst systems and processes described. The components of the catalyst systems according to the present disclosure and used in the polymerization processes of the present disclosure, as well as the resulting polymers, are described in more detail below.

The present disclosure relates to activator compounds including a cation and a non-coordinating anion that can be used in olefin polymerization processes. For example, the present disclosure provides ammonium cations coupled with non-coordinating anions of group 13, such as sterically hindered borates and aluminates. Useful borate and aluminate groups of the present disclosure include perfluoronaphthalenyl and perfluorophenyl borates and aluminates. It has been discovered that activators of the present disclosure having perfluoronaphthalenyl borate or aluminate anions have improved solubility in aliphatic solvents, as compared to conventional activator compounds. Activators of the present disclosure can provide polyolefin homopolymers having a weight average molecular weight (Mw) of about 300,000 g/mol or greater and a melt temperature (Tm) of about 130° C. or greater. Further, activators having a cation having two or more C₆ to C₃₀ alkyl groups can provide enhanced activity for polymer production.

The present disclosure relates to a catalyst system including a transition metal compound and an activator compound of Formula (I), to the use of an activator compound of Formula (I) for activating a transition metal compound in a catalyst system for polymerizing olefins, and to processes for polymerizing olefins, the process including contacting under polymerization conditions one or more olefins with a catalyst system including a transition metal compound and an activator compound of Formula (I).

The present disclosure also relates to processes for polymerizing olefins including contacting, under polymerization conditions, one or more olefins with a catalyst system including a transition metal compound and an activator compound of Formula (I).

The activator compounds of Formula (I) will be further illustrated below. Combinations of cations and non-coordinating anions disclosed are suitable to be used in the processes of the present disclosure and are thus incorporated herein.

Non-Coordinating Anion (NCA) Activators

The terms “cocatalyst” and “activator” are used interchangeably and are a compound that can activate a catalyst compound by converting the neutral catalyst compound to a catalytically active catalyst compound cation. Non-coordinating anion (NCA) means an anion either that does not coordinate to the catalyst metal cation or that does coordinate to the metal cation, but only weakly. The term NCA is also defined to include multicomponent NCA-containing activators, such as N,N-di-isotridecylanilinium tetrakis(perfluoronaphthalenyl)borate, that contain an acidic cationic group and the non-coordinating anion. The term NCA is also defined to include neutral Lewis acids, such as tris(pentafluoronaphthalenyl)boron, that can react with a catalyst to form an activated species by abstraction of an anionic group. An NCA coordinates weakly enough that a neutral Lewis base, such as an olefinically or acetylenically unsaturated monomer can displace the NCA from the catalyst center. Metals or metalloids that can form a compatible, weakly coordinating complex may be used or contained in the non-coordinating anion. Suitable metals can include aluminum, gold, and platinum. Suitable metalloids can include boron, aluminum, phosphorus, and silicon. The term non-coordinating anion activator includes neutral activators, ionic activators, and Lewis acid activators.

“Compatible” non-coordinating anions can be those, which are not degraded to neutrality when the initially formed complex decomposes. Further, the anion will not transfer an anionic substituent or fragment to the cation to cause the cation to form a neutral transition metal compound and a neutral by-product from the anion. Non-coordinating anions useful in accordance with the present disclosure are those that are compatible, stabilize the transition metal cation in the sense of balancing its ionic charge at +1, and yet retain sufficient lability to permit displacement during polymerization.

Activators

The present disclosure provides activators, such as ammonium metallate or metalloid activator compounds, including ammonium groups with long-chain aliphatic hydrocarbyl groups combined with metallate or metalloid anions, such as borates or aluminates. When an activator of the present disclosure is used with a catalyst compound (such as a group 4 metallocene compound) in an olefin polymerization, the catalyst may have higher activity, and a polymer can be formed having a higher molecular weight, a higher melt temperature, and reduced or eliminated aromatic hydrocarbon content than polymers formed using comparable activators. In addition, it has been discovered that activators of the present disclosure are soluble in aliphatic solvent.

In one or more embodiments, a 20 wt % mixture of the activator compound in n-hexane, isohexane, cyclohexane, methylcyclohexane, or a combination thereof, forms a clear homogeneous solution at 25° C., such as a 30 wt % mixture of the compound in n-hexane, isohexane, cyclohexane, methylcyclohexane, or a combination thereof, forms a clear homogeneous solution at 25° C.

In one or more embodiments, a 20 wt % mixture of the catalyst system in n-hexane, isohexane, cyclohexane, methylcyclohexane, or a combination thereof, forms a clear homogeneous solution at 25° C., such as a 30 wt % mixture of the compound in n-hexane, isohexane, cyclohexane, methylcyclohexane, or a combination thereof, forms a clear homogeneous solution at 25° C.

In embodiments of the present disclosure, the activators described have a solubility of more than 10 mM (or more than 20 mM, or more than 50 mM) at 25° C. (stirred 2 hours) in methylcyclohexane.

In embodiments of the present disclosure, the activators described have a solubility of more than 1 mM (or more than 10 mM, or more than 20 mM) at 25° C. (stirred 2 hours) in isohexane.

In embodiments of the present disclosure, the activators described have a solubility of more than 10 mM (or more than 20 mM, or more than 50 mM) at 25° C. (stirred 2 hours) in methylcyclohexane and a solubility of more than 1 mM (or more than 10 mM, or more than 20 mM) at 25° C. (stirred 2 hours) in isohexane.

In embodiments of the present disclosure, the catalyst systems described, absent insoluble supports (such as silica), have a solubility of more than 10 mM (or more than 20 mM, or more than 50 mM) at 25° C. (stirred 2 hours) in methylcyclohexane.

In embodiments of the present disclosure, the catalyst systems described, absent insoluble supports (such as silica), have a solubility of more than 1 mM (or more than 10 mM, or more than 20 mM) at 25° C. (stirred 2 hours) in isohexane.

In embodiments of the present disclosure, the catalyst systems described, absent insoluble supports (such as silica), have a solubility of more than 10 mM (or more than 20 mM, or more than 50 mM) at 25° C. (stirred 2 hours) in methylcyclohexane and a solubility of more than 1 mM (or more than 10 mM, or more than 20 mM) at 25° C. (stirred 2 hours) in isohexane.

The present disclosure relates to a catalyst system including a transition metal compound and an activator compound as described herein, to the use of such activator compounds for activating a transition metal compound in a catalyst system for polymerizing olefins, and to processes for polymerizing olefins, the process including contacting under polymerization conditions one or more olefins with a catalyst system including a transition metal compound and such activator compounds, where aromatic solvents, such as toluene, are absent (e.g. present at zero mol %, alternately present at less than 1 mol %, such as the catalyst system, the polymerization reaction and/or the polymer produced are free of “detectable aromatic hydrocarbon solvent,” such as toluene. For purposes of the present disclosure, “detectable aromatic hydrocarbon solvent” means 0.1 mg/m² or more as determined by gas phase chromatography. For purposes of the present disclosure, “detectable toluene” means 0.1 mg/m² or more as determined by gas phase chromatography.

The polyolefins produced may contain 0 ppm (alternately less than 1 ppm, alternately less than 1 ppb) of aromatic hydrocarbon. In some embodiments, the polyolefins produced contain 0 ppm (alternately less than 1 ppm, alternately less than 1 ppb) of toluene.

The catalyst systems used may contain 0 ppm (alternately less than 1 ppm, alternately less than 1 ppb) of aromatic hydrocarbon. In some embodiments, the catalyst systems used contain 0 ppm (alternately less than 1 ppm, alternately less than 1 ppb) of toluene.

Catalyst systems of the present disclosure may be formed by combining the catalysts with activators in any suitable manner. The catalyst systems may also be added to or generated in solution polymerization or bulk polymerization (in the monomer, i.e., little or no solvent).

The present disclosure relates to activator compounds represented by Formula (I): [Ar(E¹R¹R²H)_(x)(E²R³R⁴)_(y)][QR⁵R⁶R⁷R⁸]_(z)  (I) where:

each of E¹ and E² are nitrogen; Ar is a C₁₀-C₃₀ multicyclic aromatic hydrocarbyl group, where E¹ is a first Ar substitution located on a first ring of the multicyclic aromatic hydrocarbyl group and E² is a second Ar substitution located on a second ring of the multicyclic aromatic hydrocarbyl group;

x is 1 to 4;

y is 0 to 3;

z=x;

x+y is 2 to 6;

each of R¹, R², R³, and R⁴ are independently selected from C₁-C₄₀ aliphatic hydrocarbyl, substituted C₁-C₄₀ aliphatic hydrocarbyl, where R¹, R², R³, and R⁴ together include 15 or more carbon atoms;

Q is an element selected from group 13 of the Periodic Table of the Elements; and

each of R⁵, R⁶, R⁷, and R⁸ independently a hydride, a bridged or unbridged dialkylamido, a halide, an alkoxide, an aryloxide, a hydrocarbyl, a substituted hydrocarbyl, a halocarbyl, or a substituted halocarbyl.

In some embodiments of Formula (I), x is 1 and y is 1; x is 2 and y is 1; x is 2 and y is 0; x is 1 and y is 2; or x is 3 and y is 0. In at least one embodiment of Formula (I), x is 1 and y is 1, or x is 2 and y is O.

In some embodiments of Formula (I), Ar is naphthalene, or anthracene. In at least one embodiment of Formula (I), Ar is naphthalene.

In some embodiments of Formula (I), R¹ is an optionally substituted C₁-C₁₀ aliphatic hydrocarbyl, such as methyl, ethyl, propyl, or butyl. In some embodiments of Formula (I), R¹ is methyl. In some embodiments of Formula (I), R³ is an optionally substituted C₁-C₁₀ aliphatic hydrocarbyl, such as methyl, ethyl, propyl, or butyl. In some embodiments of Formula (I), R³ is methyl. In some embodiments of Formula (I), R¹ and R³ are an optionally substituted C₁-C₁₀ aliphatic hydrocarbyl, such as methyl, ethyl, propyl, or butyl. In some embodiments of Formula (I), R¹ and R³ are methyl. In some embodiments of Formula (I), R² is an optionally substituted C₆-C₃₀ such as C₈-C₂₄, or C₁₀-C₂₀ aliphatic hydrocarbyl. In some embodiments of Formula (I), R⁴ is an optionally substituted C₆-C₃₀ such as C₈-C₂₄, or C₁₀-C₂₀ aliphatic hydrocarbyl. In some embodiments of Formula (I), R² and R⁴ are independently an optionally substituted C₆-C₃₀ such as C₈-C₂₄, or C₁₀-C₂₀ aliphatic hydrocarbyl. In some embodiments of Formula (I), R¹ is methyl and R² is an optionally substituted C₆-C₃₀ such as C₈-C₂₄, or C₁₀-C₂₀ aliphatic hydrocarbyl. In some embodiments of Formula (I), R³ is methyl and R⁴ is an optionally substituted C₆-C₃₀ such as C₈-C₂₄, or C₁₀-C₂₀ aliphatic hydrocarbyl. In some embodiments of Formula (I), R¹ and R³ are an optionally substituted C₁-C₁₀ aliphatic hydrocarbyl, such as methyl, ethyl, propyl, or butyl and R² and R⁴ are independently an optionally substituted C₆-C₃₀, such as C₈-C₂₄, or C₁₀-C₂₀ aliphatic hydrocarbyl.

In some embodiments of Formula (I), R¹ is an optionally substituted C₁-C₁₀ aliphatic hydrocarbyl, such as methyl, ethyl, propyl, or butyl and R² is an optionally substituted C₆-C₃₀ linear alkyl group, such as n-hexyl, n-heptyl, n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, n-tetracosyl, n-pentacosyl, n-hexacosyl, n-heptacosyl, n-octacosyl, n-nonacosyl, or n-tricontyl. In some embodiments of Formula (I), R¹ and R² are independently an optionally substituted C₆-C₂₄ linear alkyl group, such as n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, or n-tetracosyl. In some embodiments of Formula (I), R¹ and R² are independently an optionally substituted C₆-C₂₄ linear alkyl group, such as n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, or n-tetracosyl.

In some embodiments of Formula (I), R³ is an optionally substituted C₁-C₁₀ aliphatic hydrocarbyl, such as methyl, ethyl, propyl, or butyl, and R⁴ is an optionally substituted C₆-C₃₀ linear alkyl group, such as n-hexyl, n-heptyl, n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, n-tetracosyl, n-pentacosyl, n-hexacosyl, n-heptacosyl, n-octacosyl, n-nonacosyl, or n-tricontyl. In some embodiments of Formula (I), R³ and R⁴ are independently an optionally substituted C₆-C₂₄ linear alkyl group, such as n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, or n-tetracosyl. In some embodiments of Formula (I), R³ and R⁴ are independently an optionally substituted C₆-C₂₄ linear alkyl group, such as n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, or n-tetracosyl.

In some embodiments of Formula (I), R¹ and R³ are independently an optionally substituted C₁-C₁₀ aliphatic hydrocarbyl, such as methyl, ethyl, propyl, or butyl; and R² and R⁴ are independently an optionally substituted C₆-C₃₀ linear alkyl group, such as n-hexyl, n-heptyl, n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, n-tetracosyl, n-pentacosyl, n-hexacosyl, n-heptacosyl, n-octacosyl, n-nonacosyl, or n-tricontyl. In some embodiments of Formula (I), R¹, R², R³, and R⁴ are independently an optionally substituted C₆-C₃₀ linear alkyl group, such as n-hexyl, n-heptyl, n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, n-tetracosyl, n-pentacosyl, n-hexacosyl, n-heptacosyl, n-octacosyl, n-nonacosyl, or n-tricontyl. In some embodiments of Formula (I), R¹ is methyl and R², R³, and R⁴ are independently an optionally substituted C₆-C₃₀ linear alkyl group, such as n-hexyl, n-heptyl, n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, n-tetracosyl, n-pentacosyl, n-hexacosyl, n-heptacosyl, n-octacosyl, n-nonacosyl, or n-tricontyl. In some embodiments of Formula (I), R³ is methyl and R¹, R², and R⁴ are independently an optionally substituted C₆-C₃₀ linear alkyl group, such as n-hexyl, n-heptyl, n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, n-tetracosyl, n-pentacosyl, n-hexacosyl, n-heptacosyl, n-octacosyl, n-nonacosyl, or n-tricontyl.

In some embodiments of Formula (I), R² is an optionally substituted C₁₈ aliphatic hydrocarbyl. In some embodiments of Formula (I), R⁴ is an optionally substituted C₁₈ aliphatic hydrocarbyl. In some embodiments of Formula (I), R² and R⁴ are independently an optionally substituted C₁₈ aliphatic hydrocarbyl. In some embodiments of Formula (I), R¹ is methyl and R² is an optionally substituted C₁₈ linear aliphatic hydrocarbyl. In some embodiments of Formula (I), R³ is methyl and R⁴ is an optionally substituted C₁₈ linear aliphatic hydrocarbyl. In some embodiments of Formula (I), R¹ and R³ are methyl and R² and R⁴ are independently an optionally substituted C₁₈ linear aliphatic hydrocarbyl.

In some embodiments of Formula (I), each of R⁵, R⁶, R⁷, and R⁸ is independently a C₆-C₂₄ hydrocarbyl or a substituted C₆-C₂₄ hydrocarbyl. In some embodiments of Formula (I), each of R⁵, R⁶, R⁷, and R⁸ is a fluorinated C₆-C₂₄ hydrocarbyl group. In some embodiments of Formula (I), each of R⁵, R⁶, R⁷, and R⁸ is independently a C₆-C₂₄ aromatic hydrocarbyl or a substituted C₆-C₂₄ aromatic hydrocarbyl. In some embodiments of Formula (I), each of R⁵, R⁶, R⁷, and R⁸ is a C₆-C₂₄ fluorinated aromatic hydrocarbyl group. In some embodiments of Formula (I), each of R⁵, R⁶, R⁷, and R⁸ is a C₆-C₂₄ perfluorinated aromatic hydrocarbyl group, such as pentafluorophenyl or heptafluoronaphthalenyl. In some embodiments of Formula (I), all of R⁵, R⁶, R⁷, and R⁸ are a substituted phenyl, such as pentafluorophenyl. In some embodiments of Formula (I), at least one of R⁵, R⁶, R⁷, and R⁸ is not a substituted phenyl, such as pentafluorophenyl. In at least one embodiment of Formula (I), all of R⁵, R⁶, R⁷, and R⁸ are not a substituted phenyl, such as pentafluorophenyl. In some embodiments of Formula (I), all of R⁵, R⁶, R⁷, and R⁸ are a substituted naphthalenyl, such as heptafluoronaphthalenyl. Additionally, further examples of suitable [QR⁵R⁶R⁷R⁸] include diboron compounds as disclosed in U.S. Pat. No. 5,447,895, incorporated by reference.

In some embodiments of Formula (I), R¹ is not methyl, R² is not C₁₈ alkyl and R³ is not C₁₈ alkyl, alternately R¹ is not methyl, R² is not C₁₈ alkyl and R³ is not C₁₈ alkyl and at least one R⁵, R⁶, R⁷, and R⁸ is not substituted phenyl, such as all R⁵, R⁶, R⁷, and R⁸ are not substituted phenyl.

In some embodiments of Formula (I), R¹, R², R³, and R⁴ together include 15 or more carbon atoms, such as 18 or more carbon atoms, such as 20 or more carbon atoms, such as 22 or more carbon atoms, such as 25 or more carbon atoms, such as 30 or more carbon atoms, such as 35 or more carbon atoms, such as 37 or more carbon atoms, such as 40 or more carbon atoms, such as 45 or more carbon atoms, such as 15 to 100 carbon atoms, such as 23 to 75 carbon atoms, such as 38 to 70 carbon atoms.

In some embodiments the activator is selected from the group consisting of:

1

2

3

4

5

6

7

8

9

10

11

12

13

14

15

16

17

18

19

20

21

22

23

24

25

26

27

28

29

30

31

32

33

34

35

36

37

38

39

40

41

42

43

44

45

46

47

48

49

50

51

52

53

54

55

56

57

58

59

60

61

62

63

64

In some embodiments the activator is selected from the group consisting of:

1

2

3

4

5

6

7

8

9

10

11

12

13

14

15

16

Both the cation part of Formula (I) as well as the anion part thereof, which is an NCA, will be further illustrated below. Combinations of cations and NCAs disclosed are suitable to be used in the processes of the present disclosure and are thus incorporated herein.

Activators—The Cations

The cation component of the activators described (such as those of Formula (I) above), is a protonated Lewis base that can be capable of protonating a moiety, such as an alkyl or aryl, from the transition metal compound. Thus, upon release of a neutral leaving group (e.g. an alkane resulting from the combination of a proton donated from the cationic component of the activator and an alkyl substituent of the transition metal compound) a transition metal cation results, which is the catalytically active species. The cation component of the activators described may be a monocation, dication, trication, or tetracation.

In some embodiments of Formula (I), the cation is [Ar(E¹R¹R²H)_(x)(E²R³R⁴)_(y)], and Ar is a C₁₀-C₃₀ multicyclic aromatic hydrocarbyl group, each of E¹ and E² are nitrogen; Ar is a C₁₀-C₃₀ multicyclic aromatic hydrocarbyl group, where E¹ is a first Ar substitution located on a first ring of the multicyclic aromatic hydrocarbyl group and E² is a second Ar substitution located on a second ring of the multicyclic aromatic hydrocarbyl group; x is 1 to 4; y is 0 to 3; x+y is 2 to 6; each of E¹ and E² are nitrogen; and each of R¹, R², R³, and R⁴ are independently selected from C₁-C₄₀ aliphatic hydrocarbyl, substituted C₁-C₄₀ aliphatic hydrocarbyl, where R¹, R², R³, and R⁴ together include 15 or more carbon atoms.

In some embodiments of Formula (I), R¹, R², R³, and R⁴ of the cation together include 15 or more carbon atoms, such as 18 or more carbon atoms, such as 20 or more carbon atoms, such as 22 or more carbon atoms, such as 25 or more carbon atoms, such as 30 or more carbon atoms, such as 35 or more carbon atoms, such as 37 or more carbon atoms, such as 40 or more carbon atoms, such as 45 or more carbon atoms such as 15 to 100 carbon atoms, such as 23 to 75 carbon atoms, such as 38 to 70 carbon atoms.

In some embodiments of the cation of Formula (I), Ar is naphthalene, or anthracene. In at least one embodiment of Formula (I), Ar is naphthalene.

In some embodiments of the cation of Formula (I), R¹ is an optionally substituted C₁-C₁₀ aliphatic hydrocarbyl, such as methyl, ethyl, propyl, or butyl. In some embodiments of the cation of Formula (I), R¹ is methyl. In some embodiments of the cation of Formula (I), R³ is an optionally substituted C₁-C₁₀ aliphatic hydrocarbyl, such as methyl, ethyl, propyl, or butyl. In some embodiments of the cation of Formula (I), R³ is methyl. In some embodiments of the cation of Formula (I), R¹ and R³ are an optionally substituted C₁-C₁₀ aliphatic hydrocarbyl, such as methyl, ethyl, propyl, or butyl. In some embodiments of the cation of Formula (I), R¹ and R³ are methyl. In some embodiments of the cation of Formula (I), R² is an optionally substituted C₆-C₃₀, such as C₈-C₂₄, or C₁₀-C₂₀ aliphatic hydrocarbyl. In some embodiments of the cation of Formula (I), R⁴ is an optionally substituted C₆-C₃₀, such as C₈-C₂₄, or C₁₀-C₂₀ aliphatic hydrocarbyl. In some embodiments of the cation of Formula (I), R² and R⁴ are independently an optionally substituted C₆-C₃₀, such as C₈-C₂₄, or C₁₀-C₂₀ aliphatic hydrocarbyl. In some embodiments of the cation of Formula (I), R¹ is methyl and R² is an optionally substituted C₆-C₃₀, such as C₈-C₂₄, or C₁₀-C₂₀ aliphatic hydrocarbyl. In some embodiments of the cation of Formula (I), R³ is methyl and R⁴ is an optionally substituted C₆-C₃₀, such as C₈-C₂₄, or C₁₀-C₂₀ aliphatic hydrocarbyl. In some embodiments of the cation of Formula (I), R¹ and R³ are an optionally substituted C₁-C₁₀ aliphatic hydrocarbyl, such as methyl, ethyl, propyl, or butyl; and R² and R⁴ are independently an optionally substituted C₆-C₃₀, such as C₈-C₂₄, or C₁₀-C₂₀ aliphatic hydrocarbyl.

In some embodiments of the cation of Formula (I), R¹ is an optionally substituted C₁-C₁₀ aliphatic hydrocarbyl, such as methyl, ethyl, propyl, or butyl and R² is an optionally substituted C₆-C₃₀ linear alkyl group, such as n-hexyl, n-heptyl, n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, n-tetracosyl, n-pentacosyl, n-hexacosyl, n-heptacosyl, n-octacosyl, n-nonacosyl, or n-tricontyl. In some embodiments of the cation of Formula (I), R¹ and R² are independently an optionally substituted C₆-C₂₄ linear alkyl group, such as n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, or n-tetracosyl. In some embodiments of the cation of Formula (I), R¹ and R² are independently an optionally substituted C₆-C₂₄ linear alkyl group, such as n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, or n-tetracosyl.

In some embodiments of the cation of Formula (I), R³ is an optionally substituted C₁-C₁₀ aliphatic hydrocarbyl, such as methyl, ethyl, propyl, or butyl, and R⁴ is an optionally substituted C₆-C₃₀ linear alkyl group, such as n-hexyl, n-heptyl, n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, n-tetracosyl, n-pentacosyl, n-hexacosyl, n-heptacosyl, n-octacosyl, n-nonacosyl, or n-tricontyl. In some embodiments of the cation of Formula (I), R³ and R⁴ are independently an optionally substituted C₆-C₂₄ linear alkyl group, such as n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, or n-tetracosyl. In some embodiments of the cation of Formula (I), R³ and R⁴ are independently an optionally substituted C₆-C₂₄ linear alkyl group, such as n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, or n-tetracosyl.

In some embodiments of the cation of Formula (I), R¹ and R³ are independently an optionally substituted C₁-C₁₀ aliphatic hydrocarbyl, such as methyl, ethyl, propyl, or butyl; and R² and R⁴ are independently an optionally substituted C₆-C₃₀ linear alkyl group, such as n-hexyl, n-heptyl, n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, n-tetracosyl, n-pentacosyl, n-hexacosyl, n-heptacosyl, n-octacosyl, n-nonacosyl, or n-tricontyl. In some embodiments of the cation of Formula (I), R¹, R², R³, and R⁴ are independently an optionally substituted C₆-C₃₀ linear alkyl group, such as n-hexyl, n-heptyl, n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, n-tetracosyl, n-pentacosyl, n-hexacosyl, n-heptacosyl, n-octacosyl, n-nonacosyl, or n-tricontyl. In some embodiments of the cation of Formula (I), R¹ is methyl and R², R³, and R⁴ are independently an optionally substituted C₆-C₃₀ linear alkyl group, such as n-hexyl, n-heptyl, n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, n-tetracosyl, n-pentacosyl, n-hexacosyl, n-heptacosyl, n-octacosyl, n-nonacosyl, or n-tricontyl. In some embodiments of the cation of Formula (I), R³ is methyl and R¹, R², and R⁴ are independently an optionally substituted C₆-C₃₀ linear alkyl group, such as n-hexyl, n-heptyl, n-octyl, n-nonyl, n-decyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl, n-eicosyl, n-henicosyl, n-docosyl, n-tricosyl, n-tetracosyl, n-pentacosyl, n-hexacosyl, n-heptacosyl, n-octacosyl, n-nonacosyl, or n-tricontyl.

In some embodiments of the cation of Formula (I), R² is an optionally substituted C₁₈ aliphatic hydrocarbyl. In some embodiments of the cation of Formula (I), R⁴ is an optionally substituted C₁₈ aliphatic hydrocarbyl. In some embodiments of the cation of Formula (I), R² and R⁴ are independently an optionally substituted C₁₈ aliphatic hydrocarbyl. In some embodiments of the cation of Formula (I), R¹ is methyl and R² is an optionally substituted C₁₈ linear aliphatic hydrocarbyl. In some embodiments of the cation of Formula (I), R³ is methyl and R⁴ is an optionally substituted C₁₈ linear aliphatic hydrocarbyl. In some embodiments of the cation of Formula (I), R¹ and R³ are methyl and R² and R⁴ are independently an optionally substituted C₁₈ linear aliphatic hydrocarbyl.

In some embodiments, the activator is a compound represented by Formula (I): [Ar(E¹R¹R²H)_(x)(E²R³R⁴)_(y)][QR⁵R⁶R⁷R⁸]_(z)  (I) where:

Q is an element selected from group 13 of the Periodic Table of the Elements; each of R⁵, R⁶, R⁷, and R⁸ is independently a hydride, bridged or unbridged dialkylamido, halide, alkoxide, aryloxide, hydrocarbyl, substituted hydrocarbyl, halocarbyl, or substituted halocarbyl; and the [Ar(E¹R¹R²H)_(x)(E²R³R⁴)_(y)] is selected from the group consisting of:

1

2

3

4

5

6

7

8

9

10

11

12

13

14

15

16

17

18

19

20

21

22

23

24

25

26

27

28

29

30

31

32

In some embodiments, the activator is a compound represented by Formula (I): [Ar(E¹R¹R²H)_(x)(E²R³R⁴)_(y)][QR⁵R⁶R⁷R⁸]_(z)  (I) where:

Q is an element selected from group 13 of the Periodic Table of the Elements; each of R⁵, R⁶, R⁷, and R⁸ is independently a hydride, bridged or unbridged dialkylamido, halide, alkoxide, aryloxide, hydrocarbyl, substituted hydrocarbyl, halocarbyl, or substituted halocarbyl; and the [Ar(E¹R¹R²H)_(x)(E²R³R⁴)_(y)] is selected from the group consisting of:

1

2

3

4

5

6

7

8

Activators—The Anion

The anion component of the activators include those represented by [QR⁵R⁶R⁷R⁸]⁻ where Q is an element selected from group 13 of the Periodic Table of the Elements, such as boron or aluminum, and each of R⁵, R⁶, R⁷, and R⁸ is independently a hydride, a bridged or unbridged dialkylamido, a halide, an alkoxide, an aryloxide, a hydrocarbyl, a substituted hydrocarbyl, a halocarbyl, or a substituted halocarbyl.

In some embodiments, each of R⁵, R⁶, R⁷, and R⁸ is independently a C₁-C₂₄ alkoxide, aryloxide, hydrocarbyl, substituted hydrocarbyl, halocarbyl, or substituted halocarbyl. In some embodiments, each of R⁵, R⁶, R⁷, and R⁸ is independently a C₁-C₂₄ hydrocarbyl or a C₁-C₂₄ substituted hydrocarbyl.

In some embodiments, each of R⁵, R⁶, R⁷, and R⁸ is independently a C₁-C₂₄ fluorinated hydrocarbyl group. In some embodiments, each of R⁵, R⁶, R⁷, and R⁸ is independently a C₆-C₂₄ fluorinated aryl group, such as a perfluorinated aryl group. In at least one embodiment, each of R⁵, R⁶, R⁷, and R⁸ is naphthalenyl, where at least one of R⁵, R⁶, R⁷, and R⁸ is substituted with from one to seven fluorine atoms. In some embodiments, each of R⁵, R⁶, R⁷, and R⁸ is independently naphthalenyl including one fluorine atom, two fluorine atoms, three fluorine atoms, four fluorine atoms, five fluorine atoms, six fluorine atoms, or seven fluorine atoms. In some embodiments, each R⁵, R⁶, R⁷, and R⁸ are independently perfluorinated phenyl. In some embodiments, each R⁵, R⁶, R⁷, and R⁸ are independently perfluorinated biphenyl. In some embodiments, each R⁵, R⁶, R⁷, and R⁸ are independently perfluorinated naphthalenyl.

In at least one embodiment, R⁵ is independently naphthalenyl including one fluorine atom, two fluorine atoms, three fluorine atoms, four fluorine atoms, five fluorine atoms, six fluorine atoms, or seven fluorine atoms, and each of R⁶, R⁷, and R⁸ is independently phenyl including one fluorine atom, two fluorine atoms, three fluorine atoms, four fluorine atoms, or five fluorine atoms or naphthalenyl including one fluorine atom, two fluorine atoms, three fluorine atoms, four fluorine atoms, five fluorine atoms, six fluorine atoms, or seven fluorine atoms.

In some embodiments, each R⁵, R⁶, R⁷, and R⁸ are independently perfluorinated phenyl. In some embodiments, each R⁵, R⁶, R⁷, and R⁸ are independently perfluorinated biphenyl. In some embodiments, each R⁵, R⁶, R⁷, and R⁸ are independently perfluorinated naphthalenyl. In some embodiments, the anion of the activator is tetrakis(heptafluoronaphth-2-yl)borate. In some embodiments, the anion of the activator is tetrakis(pentafluorophenyl)borate.

Anions for use in the non-coordinating anion activators described include those represented by Formula (II) below:

where:

Q* is a group 13 atom, such as B or Al;

each R¹¹ is, independently, a halide, such as a fluoride;

each R¹² is, independently, a halide, a C₆ to C₂₀ substituted aromatic hydrocarbyl group or a siloxy group of the formula —O—Si—R^(a), where R^(a) is a C₁ to C₂₀ hydrocarbyl or hydrocarbylsilyl group. n some embodiments, R¹² is a fluoride or a perfluorinated phenyl group;

each R¹³ is a halide, a C₆ to C₂₀ substituted aromatic hydrocarbyl group or a siloxy group of the formula —O—Si—R^(a), where R^(a) is a C₁ to C₂₀ hydrocarbyl or hydrocarbylsilyl group. In some embodiments, R¹³ is a fluoride or a C₆ perfluorinated aromatic hydrocarbyl group;

where R¹² and R¹³ can form one or more saturated or unsaturated, substituted or unsubstituted rings, such as R¹² and R¹³ form a perfluorinated phenyl ring. In some embodiments, the anion has a molecular weight of greater than 700 g/mol, and, at least three of the substituents on the Q* atom each have a molecular volume of greater than 180 cubic A.

“Molecular volume” is used as an approximation of spatial steric bulk of an activator molecule in solution. Comparison of substituents with differing molecular volumes allows the substituent with the smaller molecular volume to be considered “less bulky” in comparison to the substituent with the larger molecular volume. Conversely, a substituent with a larger molecular volume may be considered “more bulky” than a substituent with a smaller molecular volume.

Molecular volume may be calculated as reported in Girolami, G. S. (1994) “A Simple “Back of the Envelope” Method for Estimating the Densities and Molecular Volumes of Liquids and Solids,” Journal of Chemical Education, v.71(11), November 1994, pp. 962-964. Molecular volume (MV), in units of cubic Å, is calculated using the formula: MV=8.3V_(S), where V_(S) is the scaled volume. V_(S) is the sum of the relative volumes of the constituent atoms, and is calculated from the molecular formula of the substituent using Table A below of relative volumes. For fused rings, the V_(S) is decreased by 7.5% per fused ring. The Calculated Total MV of the anion is the sum of the MV per substituent, for example, the MV of perfluorophenyl is 183 Å³, and the Calculated Total MV for tetrakis(perfluorophenyl)borate is four times 183 Å³, or 732 Å³.

TABLE A Element Relative Volume H 1 1^(st) short period, Li to F 2 2^(nd) short period, Na to Cl 4 1^(st) long period, K to Br 5 2^(nd) long period, Rb to I 7.5 3^(rd) long period, Cs to Bi 9

Exemplary anions and their respective scaled volumes and molecular volumes are shown in Table 2 below. The dashed bonds indicate bonding to boron.

TABLE 2 Molecular MV Calculated Formula of Per Total Each subst. MV Ion Structure of Boron Substituents Substituent V_(S) (Å³) (Å³) tetrakis(perfluorophenyl)borate

C₆F₅ 22 183 732 tris(perfluorophenyl)- (perfluoronaphthalenyl)borate

 

C₆F₅ C₁₀F₇ 22 34 183 261 810 (perfluorophenyl)tris- (perfluoronaphthalenyl)borate

 

C₆F₅ C₁₀F₇ 22 34 183 261 966 tetrakis(perfluoronaphthalenyl)borate

C₁₀F₇ 34 261 1044 tetrakis(perfluorobiphenyl)borate

C₁₂F₉ 42 349 1396 [(C₆F₃(C₆F₅)₂)₄B]

C₁₈F₁₃ 62 5 2060

The activators may be added to a polymerization in the form of an ion pair using where the cation reacts with a basic leaving group on the transition metal complex to form a transition metal complex cation and [NCA]. Alternatively, the transition metal complex may be reacted with a neutral NCA precursor, such as B(C₁₀F₇)₃, which abstracts an anionic group from the complex to form an activated species.

In at least one embodiment, the activators obtained in their salt form used for a borate activator compound are: Lithium tetrakis(heptafluoronaphthalen-2-yl)borate etherate (Li-BF28), N,N-Dimethylanilinium tetrakis(heptafluoronaphthalen-2-yl)borate (DMAH-BF28), Sodium tetrakis(heptafluoronaphthalen-2-yl)borate (Na-BF28) and N,N-dimethylanilinium tetrakis(heptafluoronaphthalen-2-yl)borate (DMAH-BF28).

Examples of additional suitable anions include diboron compounds as disclosed in U.S. Pat. No. 5,447,895, which is incorporated herein by reference.

Catalyst System

In at least one embodiment, an activator of the present disclosure, when combined with a group 4 metallocene catalyst compound to form an active olefin polymerization catalyst, produces a higher molecular weight polymer (e.g., Mw) than comparative activators that use other borate anions.

In at least one embodiment, an activator of the present disclosure where R¹ is methyl, when combined with a group 4 metallocene to form an active olefin polymerization catalyst, produces a higher molecular weight polymer (e.g., Mw) than comparative activators that use other borate anions.

The typical activator-to-catalyst ratio, e.g., all NCA activators:catalyst ratio is about a 1:1 molar ratio. Additionally, the NCA activators: catalyst ratio may be from about 0.1:1 to about 100:1, such as from about 0.5:1 to about 200:1, from about 1:1 to about 500:1, from about 1:1 to about 1000:1. In some embodiments, the NCA activators:catalyst ration is from about 0.5:1 to about 10:1, such as 1:1 to 5:1.

It is also within the scope of the present disclosure that the catalyst compounds can be combined with combinations of alumoxanes and the activators described.

Synthesis

In at least one embodiment, the general synthesis of the activators can be performed using a two-step process. In the first step, an amine is dissolved in a solvent (e.g. hexane, cyclohexane, methylcyclohexane, ether, dichloromethane, toluene) and an excess (e.g., 1.2 molar equivalents) of hydrogen chloride is added to form a chloride salt. The salt is typically isolated by filtration from the reaction medium and dried under reduced pressure. The isolated chloride is then heated to reflux with about one molar equivalent of an alkali metal metallate or metalloid (such as a borate or aluminate) in a solvent (e.g. cyclohexane, dichloromethane, methylcyclohexane) to form a borate or aluminate along with byproduct alkali metal chloride, the latter of which can typically be removed by filtration.

In at least one embodiment, the general synthesis of the ammonium borate activators can be performed using a two-step process. In the first step, an amine is dissolved in a solvent (e.g. hexane, cyclohexane, methylcyclohexane, ether, dichloromethane, toluene) and an excess (e.g., 1.2 molar equivalents) of hydrogen chloride is added to form an ammonium chloride salt. The salt is typically isolated by filtration from the reaction medium and dried under reduced pressure. The isolated ammonium chloride is then heated to reflux with about one molar equivalent of an alkali metal borate in a solvent (e.g. cyclohexane, dichloromethane, methylcyclohexane) to form the ammonium borate along with byproduct alkali metal chloride, the latter of which can typically be removed by filtration.

In at least one embodiment, an activator of the present disclosure is soluble in an aliphatic solvent at a concentration of about 10 mM or greater, such as about 20 mM or greater, such as about 30 mM or greater, such as about 50 mM or greater, such as about 75 mM or greater, such as about 100 mM or greater, such as about 200 mM or greater, such as about 300 mM or greater. In at least one embodiment, an activator of the present disclosure dissolves in isohexane or methylcyclohexane at 25° C. to form a homogeneous solution of at least 10 mM concentration.

In at least one embodiment, the solubility of the borate or aluminate activators of the present disclosure in aliphatic hydrocarbon solvents increases with the number of aliphatic carbons in the cation group (i.e., the ammonium). In at least one embodiment, a solubility of at least 10 mM is achieved with an activator having an ammonium group of about 21 aliphatic carbon atoms or more, such as about 25 aliphatic carbons atoms or more, such as about 35 carbon atoms or more.

In at least one embodiment, the solubility of the ammonium borate activators of the present disclosure in aliphatic hydrocarbon solvents increases with the number of aliphatic carbons in the ammonium group. In at least one embodiment, a solubility of at least 10 mM is achieved with an activator having an ammonium group of about 21 aliphatic carbon atoms or more, such as about 25 aliphatic carbons atoms or more, such as about 35 carbon atoms or more.

Useful aliphatic hydrocarbon solvent can be isobutane, butane, pentane, isopentane, hexanes, isohexane, heptane, octane, dodecane, and mixtures thereof; or cyclic and alicyclic hydrocarbons, such as cyclohexane, cycloheptane, methylcyclohexane, methylcycloheptane, and mixtures thereof. In at least one embodiment, aromatics are present in the solvent at less than 1 wt %, such as less than 0.5 wt %, such as at 0 wt % based upon the weight of the solvents. The activators of the present disclosure can be dissolved in one or more additional solvents. Additional solvent includes ethereal, halogenated and N,N-dimethylformamide solvents.

In at least one embodiment, the aliphatic solvent is isohexane and/or methylcyclohexane.

Optional Scavengers or Co-Activators

In addition to these activator compounds, scavengers or co-activators may be used. Aluminum alkyl or organoaluminum compounds which may be utilized as scavengers or co-activators include, for example, trimethylaluminum, triethylaluminum, triisobutylaluminum, tri-n-hexylaluminum, tri-n-octylaluminum, and diethyl zinc.

In at least one embodiment, little or no scavenger is used in the process to produce the ethylene polymer. Scavenger (such as trialkyl aluminum) can be present at zero mol %, alternately the scavenger is present at a molar ratio of scavenger metal to transition metal of less than 100:1, such as less than 50:1, such as less than 15:1, such as less than 10:1.

Transition Metal Catalyst Compounds

A transition metal compound capable of catalyzing a reaction, such as a polymerization reaction, upon activation with an activator as described above is suitable for use in polymerization processes of the present disclosure, such as metallocenes.

In at least one embodiment, the present disclosure provides a catalyst system including a catalyst compound having a metal atom. The catalyst compound can be a metallocene catalyst compound. The metal can be a Group 3 through Group 12 metal atom, such as Group 3 through Group 10 metal atoms, or lanthanide Group atoms. The catalyst compound having a Group 3 through Group 12 metal atom can be monodentate or multidentate, such as bidentate, tridentate, or tetradentate, where a heteroatom of the catalyst, such as phosphorous, oxygen, nitrogen, or sulfur is chelated to the metal atom of the catalyst. Non-limiting examples include bis(phenolate)s. In at least one embodiment, the Group 3 through Group 12 metal atom is selected from Group 5, Group 6, Group 8, or Group 10 metal atoms. In at least one embodiment, a Group 3 through Group 10 metal atom is selected from Cr, Sc, Ti, Zr, Hf, V, Nb, Ta, Mn, Re, Fe, Ru, Os, Co, Rh, Ir, and Ni. In at least one embodiment, a metal atom is selected from Groups 4, 5, and 6 metal atoms. In at least one embodiment, a metal atom is a Group 4 metal atom selected from Ti, Zr, or Hf. The oxidation state of the metal atom can be from 0 to +7, for example +1, +2, +3, +4, or +5, for example +2, +3, or +4.

Metallocene Catalyst Compounds

A “metallocene” catalyst compound may be a transition metal catalyst compound having one, two or three, typically one or two, substituted or unsubstituted cyclopentadienyl ligands (such as substituted or unsubstituted Cp, Ind or Flu) bound to the transition metal. Metallocene catalyst compounds include metallocenes including Group 3 to Group 12 metal complexes, such as, Group 4 to Group 6 metal complexes, for example, Group 4 metal complexes. The metallocene catalyst compound of catalyst systems of the present disclosure may be unbridged metallocene catalyst compounds represented by Formula (III): Cp^(A)Cp^(B)M′X′_(n)  (III) where each Cp^(A) and Cp^(B) is independently selected from cyclopentadienyl ligands (for example, Cp, Ind, or Flu) and ligands isolobal to cyclopentadienyl, one or both Cp^(A) and Cp^(B) may contain heteroatoms, and one or both Cp^(A) and Cp^(B) may be substituted by one or more R″ groups; M′ is selected from Groups 3 through 12 atoms and lanthanide Group atoms; X′ is an anionic leaving group; n is 0 or an integer from 1 to 4; each R″ is independently selected from alkyl, substituted alkyl, heteroalkyl, alkenyl, substituted alkenyl, heteroalkenyl, alkynyl, substituted alkynyl, heteroalkynyl, alkoxy, aryloxy, alkylthio, arylthio, aryl, substituted aryl, heteroaryl, aralkyl, aralkylene, alkaryl, alkarylene, haloalkyl, haloalkenyl, haloalkynyl, heteroalkyl, heterocycle, heteroaryl, a heteroatom-containing group, hydrocarbyl, substituted hydrocarbyl, heterohydrocarbyl, silyl, boryl, phosphino, phosphine, amino, amine, ether, and thioether.

In at least one embodiment, each Cp^(A) and Cp^(B) is independently selected from cyclopentadienyl, indenyl, fluorenyl, indacenyl, tetrahydroindenyl, cyclopentaphenanthreneyl, benzindenyl, fluorenyl, octahydrofluorenyl, cyclooctatetraenyl, cyclopentacyclododecene, phenanthrindenyl, 3,4-benzofluorenyl, 9-phenylfluorenyl, 8-H-cyclopent[a]acenaphthylenyl, 7-H-dibenzofluorenyl, indeno[1,2-9]anthrene, thiophenoindenyl, thiophenofluorenyl, hydrogenated and substituted versions thereof. Each Cp^(A) and Cp^(B) may independently be indacenyl or tetrahydroindenyl.

The metallocene catalyst compound may be a bridged metallocene catalyst compound represented by Formula (IV): Cp^(A)(T)Cp^(B)M′X′_(n)  (IV) where each Cp^(A) and Cp^(B) is independently selected from cyclopentadienyl ligands (for example, Cp, Ind, or Flu) and ligands isolobal to cyclopentadienyl, where one or both Cp^(A) and Cp^(B) may contain heteroatoms, and one or both Cp^(A) and Cp^(B) may be substituted by one or more R″ groups; M′ is selected from Groups 3 through 12 atoms and lanthanide Group atoms, such as Group 4; X′ is an anionic leaving group; n is 0 or an integer from 1 to 4; (T) is a bridging group selected from divalent alkyl, divalent substituted alkyl, divalent heteroalkyl, divalent alkenyl, divalent substituted alkenyl, divalent heteroalkenyl, divalent alkynyl, divalent substituted alkynyl, divalent heteroalkynyl, divalent alkoxy, divalent aryloxy, divalent alkylthio, divalent arylthio, divalent aryl, divalent substituted aryl, divalent heteroaryl, divalent aralkyl, divalent aralkylene, divalent alkaryl, divalent alkarylene, divalent haloalkyl, divalent haloalkenyl, divalent haloalkynyl, divalent heteroalkyl, divalent heterocycle, divalent heteroaryl, a divalent heteroatom-containing group, divalent hydrocarbyl, divalent substituted hydrocarbyl, divalent heterohydrocarbyl, divalent silyl, divalent boryl, divalent phosphino, divalent phosphine, divalent amino, divalent amine, divalent ether, divalent thioether. R″ is selected from alkyl, substituted alkyl, heteroalkyl, alkenyl, substituted alkenyl, heteroalkenyl, alkynyl, substituted alkynyl, heteroalkynyl, alkoxy, aryloxy, alkylthio, arylthio, aryl, substituted aryl, heteroaryl, aralkyl, aralkylene, alkaryl, alkarylene, haloalkyl, haloalkenyl, haloalkynyl, heteroalkyl, heterocycle, heteroaryl, a heteroatom-containing group, hydrocarbyl, substituted hydrocarbyl, heterohydrocarbyl, silyl, boryl, phosphino, phosphine, amino, amine, germanium, ether, and thioether.

In at least one embodiment, each of Cp^(A) and Cp^(B) is independently selected from cyclopentadienyl, indenyl, fluorenyl, cyclopentaphenanthreneyl, benzindenyl, fluorenyl, octahydrofluorenyl, cyclooctatetraenyl, cyclopentacyclododecene, phenanthrindenyl, 3,4-benzofluorenyl, 9-phenylfluorenyl, 8-H-cyclopent[a]acenaphthylenyl, 7-H-dibenzofluorenyl, indeno[1,2-9]anthrene, thiophenoindenyl, thiophenofluorenyl, hydrogenated, and substituted versions thereof, such as cyclopentadienyl, n-propylcyclopentadienyl, indenyl, pentamethylcyclopentadienyl, tetramethylcyclopentadienyl, and n-butylcyclopentadienyl. Each Cp^(A) and Cp^(B) may independently be indacenyl or tetrahydroindenyl.

(T) is a bridging group containing at least one Group 13, 14, 15, or 16 element, in particular boron or a Group 14, 15 or 16 element, such as (T) is O, S, NR′, or SiR′₂, where each R′ is independently hydrogen or C₁-C₂₀ hydrocarbyl.

In another embodiment, the metallocene catalyst compound is represented by Formula (V): T_(y)Cp_(m)MG_(n)X_(q)  (V) where Cp is independently a substituted or unsubstituted cyclopentadienyl ligand (for example, substituted or unsubstituted Cp, Ind, or Flu) or substituted or unsubstituted ligand isolobal to cyclopentadienyl; M is a Group 4 transition metal; G is a heteroatom group represented by the formula JR*_(z) where J is N, P, O or S, and R* is a linear, branched, or cyclic C₁-C₂₀ hydrocarbyl; z is 1 or 2; T is a bridging group; y is 0 or 1; X is a leaving group; m=1, n=1, 2 or 3, q=0, 1, 2 or 3, and the sum of m+n+q is equal to the coordination number of the transition metal.

In at least one embodiment, J is N, and R* is methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, nonyl, cyclooctyl, cyclododecyl, decyl, undecyl, dodecyl, adamantyl or an isomer thereof.

In at least one embodiment, the catalyst compound is represented by Formula (VI) or Formula (VII):

where in each of Formula (VI) and Formula (VII):

M is the metal center, and is a Group 4 metal, such as titanium, zirconium or hafnium, such as zirconium or hafnium when L₁ and L₂ are present and titanium when Z is present;

n is 0 or 1;

T is an optional bridging group which, if present, is a bridging group containing at least one Group 13, 14, 15, or 16 element, in particular boron or a Group 14, 15 or 16 element (such as T is selected from dialkylsilyl, diarylsilyl, dialkylmethyl, ethylenyl (—CH₂—CH₂—) or hydrocarbylethylenyl where one, two, three or four of the hydrogen atoms in ethylenyl are substituted by hydrocarbyl, where hydrocarbyl can be independently C₁ to C₁₆ alkyl or phenyl, tolyl, xylyl and the like), and when T is present, the catalyst represented can be in a racemic or a meso form;

L₁ and L₂ are independently cyclopentadienyl, indenyl, tetrahydroindenyl or fluorenyl, optionally substituted, that are each bonded to M, or L₁ and L₂ are independently cyclopentadienyl, indenyl, tetrahydroindenyl or fluorenyl, which are optionally substituted, in which two adjacent substituents on L₁ and L₂ are optionally joined to form a substituted or unsubstituted, saturated, partially unsaturated, or aromatic cyclic or polycyclic substituent;

Z is nitrogen or phosphorus, such as nitrogen;

q is 1 or 2, such as q is 1 when Z is N;

R′ is a cyclic, linear or branched C₁ to C₄₀ alkyl or substituted alkyl group;

X₁ and X₂ are, independently, hydrogen, halogen, hydride radicals, hydrocarbyl radicals, substituted hydrocarbyl radicals, halocarbyl radicals, substituted halocarbyl radicals, silylcarbyl radicals, substituted silylcarbyl radicals, germylcarbyl radicals, or substituted germylcarbyl radicals; or X₁ and X₂ are joined and bound to the metal atom to form a metallacycle ring containing from about 3 to about 20 carbon atoms; or both together can be an olefin, diolefin or aryne ligand.

T in formulas described may be present and may be a bridging group containing at least one Group 13, 14, 15, or 16 element, such as a Group 14 element. Examples of suitable bridging groups include P(═S)R′, P(═Se)R′, P(═O)R′, R′₂C, R′₂Si, R′₂Ge, R′₂CCR′₂, R′₂CCR′₂CR′₂, R′₂CCR′₂CR′₂CR′₂, R′C═CR′, R′C═CR′CR′₂, R′₂CCR′═CR′CR′₂, R′C═CR′CR′═CR′, R′C═CR′CR′₂CR′₂, R′₂CSiR′₂, R′₂SiSiR′₂, R′₂SiOSiR′₂, R′₂CSiR′₂CR′₂, R′₂SiCR′₂SiR′₂, R′C═CR′SiR′₂, R′₂CGeR′₂, R′₂GeGeR′₂, R′₂CGeR′₂CR′₂, R′₂GeCR′₂GeR′₂, R′₂SiGeR′₂, R′C═CR′GeR′₂, R′B, R′₂C—BR′, R′₂C—BR′—CR′₂, R′₂C—O—CR′₂, R′₂CR′₂C—O—CR′₂CR′₂, R′₂C—O—CR′₂CR′₂, R′₂C—O—CR′═CR′, R′₂C—S—CR′₂, R′₂CR′₂C—S—CR′₂CR′₂, R′₂C—S—CR′₂CR′₂, R′₂C—S—CR′═CR′, R′₂C—Se—CR′₂, R′₂CR′₂C—Se—CR′₂CR′₂, R′₂C—Se—CR′₂CR′₂, R′₂C—Se—CR′═CR′, R′₂C—N═CR′, R′₂C—NR′—CR′₂, R′₂C—NR′—CR′₂CR′₂, R′₂C—NR′—CR′═CR′, R′₂CR′₂C—NR′—CR′₂CR′₂, R′₂C—P═CR′, R′₂C—PR′—CR′₂, O, S, Se, Te, NR′, PR′, As R′, SbR′, O—O, S—S, R′N—NR′, R′P—PR′, O—S, O—NR′, O—PR′, S—NR′, S—PR′, and R′N—PR′ where R′ is hydrogen or a C₁-C₂₀ containing hydrocarbyl, substituted hydrocarbyl, halocarbyl, substituted halocarbyl, silylcarbyl or germylcarbyl substituent and optionally two or more adjacent R′ may join to form a substituted or unsubstituted, saturated, partially unsaturated or aromatic, cyclic or polycyclic substituent. Examples for the bridging group T include CH₂, CH₂CH₂, SiMe₂, SiPh₂, SiMePh, Si(CH₂)₃, Si(CH₂)₄, O, S, NPh, PPh, NMe, PMe, NEt, NPr, NBu, PEt, PPr, Me₂SiOSiMe₂, and PBu.

In some embodiments of formulas described, T is represented by the formula R*₂J or (R*₂J)₂, where J is C, Si, or Ge, and each R* is, independently, hydrogen, halogen, C₁ to C₂₀ hydrocarbyl (such as methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, nonyl, decyl, undecyl, or dodecyl) or a C₁ to C₂₀ substituted hydrocarbyl, and two R^(a) can form a cyclic structure including aromatic, partially saturated, or saturated cyclic or fused ring system. T may be a bridging group including carbon or silica, such as dialkylsilyl, such as T is selected from CH₂, CH₂CH₂, C(CH₃)₂, SiMe₂, SiPh₂, SiMePh, silylcyclobutyl (Si(CH₂)₃), (Ph)₂C, (p-(Et)₃SiPh)₂C, Me₂SiOSiMe₂, and cyclopentasilylene (Si(CH₂)₄).

In at least one embodiment, the catalyst compound has a symmetry that is C₂ symmetrical.

The metallocene catalyst component may include a combination of “embodiments” described.

Suitable metallocenes include, but are not limited to, the metallocenes disclosed and referenced in the US patents cited above, as well as those disclosed and referenced in U.S. Pat. Nos. 7,179,876; 7,169,864; 7,157,531; 7,129,302; 6,995,109; 6,958,306; 6,884,748; 6,689,847; US Patent publication 2007/0055028, and published PCT Applications WO 1997/022635; WO 2000/699022; WO 2001/030860; WO 2001/030861; WO 2002/046246; WO 2002/050088; WO 2004/026921; and WO 2006/019494, all incorporated herein by reference. Additional catalysts include those referenced in U.S. Pat. Nos. 6,309,997; 6,265,338; US Patent publication 2006/019925, and the following articles: Resconi, L. et al. (2000) “Selectivity in Propene Polymerization with Metallocene Catalysts,” Chem. Rev., v.100(4), pp. 1253-1346; Gibson, V. C. et al. (2003) “Advances in Non-Metallocene Olefin Polymerization Catalysis,” Chem. Rev., v.103(1), pp. 283-316; Chem Eur. J. 2006, v.12, p. 7546; Nakayama, Y et al. (2004), “Olefin Polymerization Behavior of bis(phenoxy-imine) Zr, Ti, and V complexes with MgCl₂-based Cocatalysts,” J. Mol. Catalysis A: Chemical, v.213, pp. 141-150; Nakayama, Y. et al. (2005), Propylene Polymerization Behavior of Fluorinated Bis(phenoxy-imine) Ti Complexes with an MgCl₂-Based Compound (MgCl₂—Supported Ti-Based Catalysts),” Macromol. Chem. Phys., v.206(18), pp. 1847-1852; and Matsui, S. et al. (2001) “A Family of Zirconium Complexes Having Two Phenoxy-Imine Chelate Ligands for Olefin Polymerization,” J. Am. Chem. Soc., v.123(28), pp. 6847-6856.

Exemplary metallocene compounds include:

-   bis(cyclopentadienyl)zirconium dichloride, -   bis(n-butylcyclopentadienyl)zirconium dichloride, -   bis(n-butylcyclopentadienyl)zirconium dimethyl, -   bis(pentamethylcyclopentadienyl)zirconium dichloride, -   bis(pentamethylcyclopentadienyl)zirconium dimethyl, -   bis(pentamethylcyclopentadienyl)hafnium dichloride, -   bis(pentamethylcyclopentadienyl)zirconium dimethyl, -   bis(1-methyl-3-n-butylcyclopentadienyl)zirconium dichloride, -   bis(1-methyl-3-n-butylcyclopentadienyl)zirconium dimethyl, -   bis(1-methyl-3-n-butylcyclopentadienyl)hafnium dichloride, -   bis(1-methyl-3-n-butylcyclopentadienyl)zirconium dimethyl, -   bis(indenyl)zirconium dichloride, bis(indenyl)zirconium dimethyl, -   bis(tetrahydro-1-indenyl)zirconium dichloride, -   bis(tetrahydro-1-indenyl)zirconium dimethyl, -   (n-propyl cyclopentadienyl, pentamethyl cyclopentadienyl)zirconium     dichloride, and -   (n-propyl cyclopentadienyl, pentamethyl cyclopentadienyl)zirconium     dimethyl.

In at least one embodiment, the catalyst compound may be selected from:

-   dimethylsilylbis(tetrahydroindenyl)MX_(n), -   dimethylsilyl bis(2-methylindenyl)MX_(n), -   dimethylsilyl bis(2-methylfluorenyl)MX_(n), -   dimethylsilyl bis(2-methyl-5,7-propylindenyl)MX_(n), -   dimethylsilyl bis(2-methyl-4-phenylindenyl)MX_(n), -   dimethylsilyl bis(2-ethyl-5-phenylindenyl)MX_(n), -   dimethylsilyl bis(2-methyl-4-biphenylindenyl)MX_(n), -   dimethylsilylene bis(2-methyl-4-carbazolylindenyl)MX_(n), -   rac-dimethylsilyl-bis-(5,6,7,8-tetrahydro-5,5,8,8-tetramethyl-2-methyl-1H-benz(f)indene)MX_(n), -   diphenylmethylene (cyclopentadienyl)(fluoreneyl)MX_(n), -   bis(methylcyclopentadienyl)MX_(n), -   rac-dimethylsiylbis(2-methyl,3-propyl indenyl)MX_(n), -   dimethylsilylbis(indenyl)MX_(n), -   Rac-meso-diphenylsilyl-bis(n-propylcyclopentadienyl)MX_(n), -   1,     1′-bis(4-triethylsilylphenyl)methylene-(cyclopentadienyl)(3,8-di-tertiary-butyl-1-fluorenyl)MX_(n)     (bridge is considered the 1 position), -   bis-trimethylsilylphenyl-methylene(cyclopentadienyl)(di-t-butylfluorenyl)MXn, -   bis-trimethylsilylphenyl-methylene(cyclopentadienyl)(fluorenyl)MXn, -   bisphenylmethylene(cyclopentadienyl)(dimethylfluorenyl)MXn, -   bis(n-propylcyclopentadienyl)MX_(n), -   bis(n-butylcyclopentadienyl)MX_(n), -   bis(n-pentylcyclopentadienyl)MX_(n), -   (n-propyl cyclopentadienyl)(n-butylcyclopentadienyl)MX_(n), -   bis[(2-trimethylsilylethyl)cyclopentadienyl]MX_(n), -   bis(trimethylsilyl cyclopentadienyl)MX_(n), -   dimethylsilylbis(n-propylcyclopentadienyl)MX_(n), -   dimethylsilylbis(n-butylcyclopentadienyl)MX_(n), -   bis(1-n-propyl-2-methylcyclopentadienyl)MX_(n), -   (n-propylcyclopentadienyl)(1-n-propyl-3-n-butylcyclopentadienyl)MX_(n), -   bis(1-methyl, 3-n-butyl cyclopentadienyl)MX_(n), -   bis(indenyl)MX_(n), -   dimethylsilyl     (tetramethylcyclopentadienyl)(cyclododecylamido)MX_(n), -   dimethylsilyl (tetramethylcyclopentadienyl)(t-butylamido)MX_(n), -   μ-(CH₃)₂Si(cyclopentadienyl)(1-adamantylamido)MX_(n), -   μ-(CH₃)₂Si(3-tertbutylcyclopentadienyl)(1-adamantylamido)MX_(n), -   μ-(CH₃)₂(tetramethylcyclopentadienyl)(1-adamantylamido)MX_(n), -   μ-(CH₃)₂Si(tetramethylcyclopentadienyl)(1-adamantylamido)MX_(n), -   μ-(CH₃)₂C(tetramethylcyclopentadienyl)(1-adamantylamido)MX_(n), -   μ-(CH₃)₂Si(tetramethylcyclopentadienyl)(1-tertbutylamido)MX_(n), -   μ-(CH₃)₂Si(fluorenyl)(1-tertbutylamido)MX_(n), -   μ-(CH₃)₂Si(tetramethylcyclopentadienyl)(1-cyclododecylamido)MX_(n), -   μ-(C₆H₅)₂C(tetramethylcyclopentadienyl)(1-cyclododecylamido)MX_(n), -   μ-(CH₃)₂Si(η⁵-2,6,6-trimethyl-1,5,6,7-tetrahydro-s-indacen-1-yl)(tertbutylamido)MX_(n),     where M is selected from Ti, Zr, and Hf; where X is selected from     the group consisting of halogens, hydrides, C₁₋₁₂ alkyls, C₂₋₁₂     alkenyls, C₆₋₁₂ aryls, C₇₋₂₀ alkylaryls, C₁₋₁₂ alkoxys, C₆₋₁₆     aryloxys, C₇₋₁₈ alkylaryloxys, C₁₋₁₂ fluoroalkyls, C₆₋₁₂     fluoroaryls, and C₁₋₁₂ heteroatom-containing hydrocarbons,     substituted derivatives thereof, and combinations thereof, and where     n is zero or an integer from 1 to 4. In some embodiments, X is     selected from halogens (such as bromide, fluoride, chloride), or C₁     to C₂₀ alkyls (such as methyl, ethyl, propyl, butyl, and pentyl) and     n is 1 or 2, typically 2.

In some embodiments, the catalyst is one or more of:

-   bis(1-methyl, 3-n-butyl cyclopentadienyl) M(R)₂; -   dimethylsilyl bis(indenyl)M(R)₂; -   bis(indenyl)M(R)₂; -   dimethylsilyl bis(tetrahydroindenyl)M(R)₂; -   bis(n-propylcyclopentadienyl)M(R)₂; -   dimethylsilyl (tetramethylcyclopentadienyl)(cyclododecylamido)M(R)₂; -   dimethylsilyl (tetramethylcyclopentadienyl)(cyclododecylamido)M(R)₂; -   dimethylsilyl (tetramethylcyclopentadienyl)(t-butylamido)M(R)₂; -   dimethylsilyl (tetramethylcyclopentadienyl)(t-butylamido)M(R)₂; -   μ-(CH₃)₂Si(cyclopentadienyl)(1-adamantylamido)M(R)₂; -   μ-(CH₃)₂Si(3-tertbutylcyclopentadienyl)(1-adamantylamido)M(R)₂; -   μ-(CH₃)₂(tetramethylcyclopentadienyl)(1-adamantylamido)M(R)₂; -   μ-(CH₃)₂Si(tetramethylcyclopentadienyl)(1-adamantylamido)M(R)₂; -   μ-(CH₃)₂C(tetramethylcyclopentadienyl)(1-adamantylamido)M(R)₂; -   μ-(CH₃)₂Si(tetramethylcyclopentadienyl)(1-tertbutylamido)M(R)₂; -   μ-(CH₃)₂Si(fluorenyl)(1-tertbutylamido)M(R)₂; -   μ-(CH₃)₂Si(tetramethylcyclopentadienyl)(1-cyclododecylamido)M(R)₂; -   μ-(C₆H₅)₂C(tetramethylcyclopentadienyl)(1-cyclododecylamido)M(R)₂; -   μ-(CH₃)₂Si(η⁵-2,6,6-trimethyl-1,5,6,7-tetrahydro-s-indacen-1-yl)(tertbutylamido)M(R)₂;     where M is selected from Ti, Zr, and Hf; and R is selected from     halogen or C₁ to C₅ alkyl.

In some embodiments, the catalyst compound is one or more of:

-   dimethylsilyl     (tetramethylcyclopentadienyl)(cyclododecylamido)titanium dimethyl; -   dimethylsilyl     (tetramethylcyclopentadienyl)(cyclododecylamido)titanium dimethyl; -   dimethylsilyl (tetramethylcyclopentadienyl)(t-butylamido)titanium     dimethyl; -   dimethylsilyl (tetramethylcyclopentadienyl)(t-butylamido)titanium     dimethyl; -   μ-(CH₃)₂Si(cyclopentadienyl)(1-adamantylamido)titanium dimethyl; -   μ-(CH₃)₂Si(3-tertbutylcyclopentadienyl)(1-adamantylamido)titanium     dimethyl; -   μ-(CH₃)₂(tetramethylcyclopentadienyl)(1-adamantylamido)titanium     dimethyl; -   μ-(CH₃)₂Si(tetramethylcyclopentadienyl)(1-adamantylamido)titanium     dimethyl; -   μ-(CH₃)₂C(tetramethylcyclopentadienyl)(1-adamantylamido)titanium     dimethyl; -   μ-(CH₃)₂Si(tetramethylcyclopentadienyl)(1-tertbutylamido)titanium     dimethyl₂; -   μ-(CH₃)₂Si(fluorenyl)(1-tertbutylamido)titanium dimethyl; -   μ-(CH₃)₂Si(tetramethylcyclopentadienyl)(1-cyclododecylamido)titanium     dimethyl; -   μ-(C₆H₅)₂C(tetramethylcyclopentadienyl)(1-cyclododecylamido)titanium     dimethyl; and/or -   μ-(CH₃)₂Si(η⁵-2,6,6-trimethyl-1,5,6,7-tetrahydro-s-indacen-1-yl)(tertbutylamido)titanium     dimethyl.

In at least one embodiment, the catalyst is rac-dimethylsilyl-bis(indenyl)hafnium dimethyl and or 1, 1′-bis(4-triethylsilylphenyl)methylene-(cyclopentadienyl)(3,8-di-tertiary-butyl-1-fluorenyl)hafnium dimethyl.

In at least one embodiment, the catalyst compound is one or more of:

-   bis(1-methyl, 3-n-butyl cyclopentadienyl)hafnium dimethyl, -   bis(1-methyl, 3-n-butyl cyclopentadienyl)zirconium dimethyl, -   dimethylsilyl bis(indenyl)zirconium dimethyl, -   dimethylsilyl bis(indenyl)hafnium dimethyl, -   bis(indenyl)zirconium dimethyl, -   bis(indenyl)hafnium dimethyl, -   dimethylsilyl bis(tetrahydroindenyl)zirconium dimethyl, -   bis(n-propylcyclopentadienyl)zirconium dimethyl, -   dimethylsilylbis(tetrahydroindenyl)hafnium dimethyl, -   dimethylsilyl bis(2-methylindenyl)zirconium dimethyl, -   dimethylsilyl bis(2-methylfluorenyl)zirconium dimethyl, -   dimethylsilyl bis(2-methylindenyl)hafnium dimethyl, -   dimethylsilyl bis(2-methylfluorenyl)hafnium dimethyl, -   dimethylsilyl bis(2-methyl-5,7-propylindenyl) zirconium dimethyl, -   dimethylsilyl bis(2-methyl-4-phenylindenyl) zirconium dimethyl, -   dimethylsilyl bis(2-ethyl-5-phenylindenyl) zirconium dimethyl, -   dimethylsilyl bis(2-methyl-4-biphenylindenyl) zirconium dimethyl, -   dimethylsilylene bis(2-methyl-4-carbazolylindenyl) zirconium     dimethyl, -   rac-dimethylsilyl-bis-(5,6,7,8-tetrahydro-5,5,8,8-tetramethyl-2-methyl-1H-benz(f)indene)hafnium     dimethyl, -   diphenylmethylene (cyclopentadienyl)(fluoreneyl)hafnium dimethyl, -   bis(methylcyclopentadienyl)zirconium dimethyl, -   rac-dimethylsiylbis(2-methyl,3-propyl indenyl)hafnium dimethyl, -   dimethylsilylbis(indenyl)hafnium dimethyl, -   dimethylsilylbis(indenyl)zirconium dimethyl, -   dimethyl     rac-dimethylsilyl-bis-(5,6,7,8-tetrahydro-5,5,8,8-tetramethyl-2-methyl-1H-benz(f)indene)hafnium     dimethyl, -   Rac-meso-diphenylsilyl-bis(n-propylcyclopentadienyl)hafnium     dimethyl, -   1,     1′-bis(4-triethylsilylphenyl)methylene-(cyclopentadienyl)(3,8-di-tertiary-butyl-1-fluorenyl)hafnium     X_(n) (bridge is considered the 1 position), -   bis-trimethylsilylphenyl-methylene(cyclopentadienyl)(di-t-butylfluorenyl)hafnium     dimethyl, -   bis-trimethylsilylphenyl-methylene(cyclopentadienyl)(fluorenyl)hafnium     dimethyl, -   bisphenylmethylene(cyclopentadienyl)(dimethylfluorenyl)hafnium     dimethyl, -   bis(n-propylcyclopentadienyl)hafnium dimethyl, -   bis(n-butylcyclopentadienyl)hafnium dimethyl, -   bis(n-pentylcyclopentadienyl)hafnium dimethyl, -   (n-propyl cyclopentadienyl)(n-butylcyclopentadienyl)hafnium     dimethyl, -   bis[(2-trimethylsilylethyl)cyclopentadienyl]hafnium dimethyl, -   bis(trimethylsilyl cyclopentadienyl)hafnium dimethyl, -   dimethylsilylbis(n-propylcyclopentadienyl)hafnium dimethyl, -   dimethylsilylbis(n-butylcyclopentadienyl)hafnium dimethyl, -   bis(1-n-propyl-2-methylcyclopentadienyl)hafnium dimethyl, and -   (n-propylcyclopentadienyl)(1-n-propyl-3-n-butylcyclopentadienyl)hafnium     dimethyl, -   bis(n-propylcyclopentadienyl)hafnium dimethyl, -   bis(n-butylcyclopentadienyl)hafnium dimethyl, -   bis(n-pentylcyclopentadienyl)hafnium dimethyl, -   (n-propyl cyclopentadienyl)(n-butylcyclopentadienyl)hafnium     dimethyl, -   bis[(2-trimethylsilylethyl)cyclopentadienyl]hafnium dimethyl, -   bis(trimethylsilyl cyclopentadienyl)hafnium dimethyl, -   dimethylsilylbis(n-propylcyclopentadienyl)hafnium dimethyl, -   dimethylsilylbis(n-butylcyclopentadienyl)hafnium dimethyl, -   bis(1-n-propyl-2-methylcyclopentadienyl)hafnium dimethyl, -   (n-propylcyclopentadienyl)(1-n-propyl-3-n-butylcyclopentadienyl)hafnium     dimethyl, and -   dimethylsilyl(3-n-propylcyclopentadienyl)(tetramethylcyclopentadienyl)zirconium     dimethyl.     Non-Metallocene Catalyst Compounds

Transition metal complexes for polymerization processes can include an olefin polymerization catalyst. Suitable catalyst components may include “non-metallocene complexes” that are defined to be transition metal complexes that do not feature a cyclopentadienyl anion or substituted cyclopentadienyl anion donors (e.g., cyclopentadienyl, fluorenyl, indenyl, methylcyclopentadienyl). Examples of families of non-metallocene complexes that may be suitable can include late transition metal pyridylbisimines (e.g., U.S. Pat. No. 7,087,686), group 4 pyridyldiamidos (e.g., U.S. Pat. No. 7,973,116), quinolinyldiamidos (e.g., US Pub. No. 2018/0002352 A1), pyridylamidos (e.g., U.S. Pat. No. 7,087,690), phenoxyimines (e.g., Makio, H. et al. (2009) “Development and Application of FI Catalysts for Olefin Polymerization: Unique Catalysis and Distinctive Polymer Formation,” Accounts of Chemical Research, v.42(10), pp. 1532-1544), and bridged bi-aromatic complexes (e.g., U.S. Pat. No. 7,091,292), the disclosures of which are incorporated herein by reference.

Catalyst complexes that are suitable for use in combination with the activators described include: pyridyldiamido complexes; quinolinyldiamido complexes; phenoxyimine complexes; bisphenolate complexes; cyclopentadienyl-amidinate complexes; and iron pyridyl bis(imine) complexes or a combination thereof, including a combination with metallocene complexes.

The term “pyridyldiamido complex” or “pyridyldiamide complex” or “pyridyldiamido catalyst” or “pyridyldiamide catalyst” refers to a class of coordination complexes described in U.S. Pat. No. 7,973,116B2, US 2012/0071616A1, US 2011/0224391A1, US 2011/0301310A1, US 2015/0141601A1, U.S. Pat. Nos. 6,900,321 and 8,592,615 that feature a dianionic tridentate ligand that is coordinated to a metal center through one neutral Lewis basic donor atom (e.g., a pyridine group) and a pair of anionic amido or phosphido (i.e., deprotonated amine or phosphine) donors. In these complexes the pyridyldiamido ligand is coordinated to the metal with the formation of one five membered chelate ring and one seven membered chelate ring. It is possible for additional atoms of the pyridyldiamido ligand to be coordinated to the metal without affecting the catalyst function upon activation; for example: a cyclometalated substituted aryl group that forms an additional bond to the metal center.

The term “quinolinyldiamido complex” or “quinolinyldiamido catalyst” or “quinolinyldiamide complex” or “quinolinyldiamide catalyst” refers to a related class of pyridyldiamido complex/catalyst described in US 2018/0002352 where a quinolinyl moiety is present instead of a pyridyl moiety.

The term “phenoxyimine complex” or “phenoxyimine catalyst” refers to a class of coordination complexes described in EP 0874005 that feature a monoanionic bidentate ligand that is coordinated to a metal center through one neutral Lewis basic donor atom (e.g., an imine moiety) and an anionic aryloxy (i.e., deprotonated phenoxy) donor. Typically two of these bidentate phenoxyimine ligands are coordinated to a group 4 metal to form a complex that is useful as a catalyst component.

The term “bisphenolate complex” or “bisphenolate catalyst” refers to a class of coordination complexes described in U.S. Pat. No. 6,841,502, WO 2017/004462, and WO 2006/020624 that feature a dianionic tetradentate ligand that is coordinated to a metal center through two neutral Lewis basic donor atoms (e.g., oxygen bridge moieties) and two anionic aryloxy (i.e., deprotonated phenoxy) donors.

The term “cyclopentadienyl-amidinate complex” or “cyclopentadienyl-amidinate catalyst” refers to a class of coordination complexes described in U.S. Pat. No. 8,188,200 that typically feature a group 4 metal bound to a cyclopentadienyl anion, a bidentate amidinate anion, and a couple of other anionic groups.

The term “iron pyridyl bis(imine) complex” refers to a class of iron coordination complexes described in U.S. Pat. No. 7,087,686 that typically feature an iron metal center coordinated to a neutral, tridentate pyridyl bis(imine) ligand and two other anionic ligands.

Non-metallocene complexes can include iron complexes of tridentate pyridylbisimine ligands, zirconium and hafnium complexes of pyridylamido ligands, zirconium and hafnium complexes of tridentate pyridyldiamido ligands, zirconium and hafnium complexes of tridentate quinolinyldiamido ligands, zirconium and hafnium complexes of bidentate phenoxyimine ligands, and zirconium and hafnium complexes of bridged bi-aromatic ligands.

Suitable non-metallocene complexes can include zirconium and hafnium non-metallocene complexes. In at least one embodiment, non-metallocene complexes for the present disclosure include group 4 non-metallocene complexes including two anionic donor atoms and one or two neutral donor atoms. Suitable non-metallocene complexes for the present disclosure include group 4 non-metallocene complexes including an anionic amido donor. Suitable non-metallocene complexes for the present disclosure include group 4 non-metallocene complexes including an anionic aryloxide donor atom. Suitable non-metallocene complexes for the present disclosure include group 4 non-metallocene complexes including two anionic aryloxide donor atoms and two additional neutral donor atoms.

A catalyst compounds can be a quinolinyldiamido (QDA) transition metal complex represented by Formula (VIII), such as by Formula (IX), such as by Formula (X):

where:

M is a group 3, 4, 5, 6, 7, 8, 9, 10, 11, or 12 metal, such as a group 4 metal;

J is group including a three-atom-length bridge between the quinoline and the amido nitrogen, such as a group containing up to 50 non-hydrogen atoms;

E is carbon, silicon, or germanium;

X is an anionic leaving group, (such as a hydrocarbyl group or a halogen);

L is a neutral Lewis base;

R¹ and R¹³ are independently selected from the group including of hydrocarbyls, substituted hydrocarbyls, and silyl groups;

R², R³, R⁴, R⁵, R⁶, R⁷, R⁸, R⁹, R¹⁰, R^(10′), R¹¹, R^(11′), R¹², and R¹⁴ are independently hydrogen, hydrocarbyl, alkoxy, silyl, amino, aryloxy, substituted hydrocarbyl, halogen, or phosphino;

n is 1 or 2;

m is 0, 1, or 2, where

n+m is not greater than 4; and

two R groups (e.g., R¹ & R², R² & R³, R¹⁰ and R¹¹, etc.) may be joined to form a substituted hydrocarbyl, unsubstituted hydrocarbyl, substituted heterocyclic, or unsubstituted heterocyclic, saturated or unsaturated ring, where the ring has 5, 6, 7, or 8 ring atoms and where substitutions on the ring can join to form additional rings;

two X groups may be joined together to form a dianionic group;

two L groups may be joined together to form a bidentate Lewis base; and

X group may be joined to an L group to form a monoanionic bidentate group.

In at least one embodiment of Formulas (VIII), (IX), and (X), M is a group 4 metal, such as zirconium or hafnium, such as M is hafnium.

Representative non-metallocene transition metal compounds usable for forming poly(alpha-olefin)s of the present disclosure also include tetrabenzyl zirconium, tetra bis(trimethylsilymethyl) zirconium, oxotris(trimethlsilylmethyl) vanadium, tetrabenzyl hafnium, tetrabenzyl titanium, bis(hexamethyl disilazido)dimethyl titanium, tris(trimethyl silyl methyl) niobium dichloride, and tris(trimethylsilylmethyl) tantalum dichloride.

In at least one embodiment of Formulas (VIII), (IX), and (X), J is an aromatic substituted or unsubstituted hydrocarbyl having from 3 to 30 non-hydrogen atoms, such as J is represented by the formula:

such as J is

where R⁷, R⁸, R⁹, R¹⁰, R^(10′), R¹¹, R^(11′), R¹², R¹⁴ and E are as defined above, and two R groups (e.g., R⁷ & R⁸, R⁸ & R⁹, R⁹ & R¹⁰, R¹⁰ & R¹¹, etc.) may be joined to form a substituted or unsubstituted hydrocarbyl or heterocyclic ring, where the ring has 5, 6, 7, or 8 ring atoms (such as 5 or 6 atoms), and said ring may be saturated or unsaturated (such as partially unsaturated or aromatic), such as J is an arylalkyl (such as arylmethyl, etc.) or dihydro-1H-indenyl, or tetrahydronaphthalenyl group.

In at least one embodiment of Formulas (VIII), (IX), and (X), J is selected from the following structures:

where

indicates connection to the complex.

In at least one embodiment of Formulas (VIII), (IX), and (X), E is carbon.

In some embodiments of Formulas (VIII), (IX), and (X), X may be an alkyl (such as alkyl groups having 1 to 10 carbons, such as methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, nonyl, decyl, and isomers thereof), aryl, hydride, alkylsilane, fluoride, chloride, bromide, iodide, triflate, carboxylate, amido (such as NMe₂), or alkylsulfonate.

In at least one embodiment of Formulas (VIII), (IX), and (X), L is an ether, amine or thioether.

In at least one embodiment of Formulas (VIII), (IX), and (X), R⁷ and R⁸ are joined to form a six-membered aromatic ring with the joined R⁷/R⁸ group being —CH═CHCH═CH—.

In some embodiments of Formulas (VIII), (IX), and (X), R¹⁰ and R¹¹ may be joined to form a five-membered ring with the joined R¹⁰R¹¹ group being —CH₂CH₂—.

In some embodiments of Formulas (VIII), (IX), and (X), R^(m) and R^(H) are joined to form a six-membered ring with the joined R¹⁰R¹¹ group being —CH₂CH₂CH₂—.

In some embodiments of Formulas (VIII), (IX), and (X), R¹ and R¹³ may be independently selected from phenyl groups that are variously substituted with from zero to five substituents that include F, Cl, Br, I, CF₃, NO₂, alkoxy, dialkylamino, aryl, and alkyl groups having 1 to 10 carbons, such as methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, nonyl, decyl, and isomers thereof.

In at least one embodiment, the QDA transition metal complex represented by the Formula (IX) above where:

M is a group 4 metal (such hafnium);

E is selected from carbon, silicon, or germanium (such as carbon);

X is an alkyl, aryl, hydride, alkylsilane, fluoride, chloride, bromide, iodide, triflate, carboxylate, amido, alkoxo, or alkylsulfonate;

L is an ether, amine, or thioether;

R¹ and R¹³ are independently selected from the group consisting of hydrocarbyls, substituted hydrocarbyls, and silyl groups (such as aryl);

R², R³, R⁴, R⁵, R⁶, R⁷, R⁸, R⁹, R¹⁰, R¹¹, and R¹² are independently hydrogen, hydrocarbyl, alkoxy, silyl, amino, aryloxy, substituted hydrocarbyls, halogen, and phosphino;

n is 1 or 2;

m is 0, 1, or 2;

n+m is from 1 to 4;

two X groups may be joined together to form a dianionic group;

two L groups may be joined together to form a bidentate Lewis base;

an X group may be joined to an L group to form a monoanionic bidentate group;

R⁷ and R⁸ may be joined to form a ring (such as an aromatic ring, a six-membered aromatic ring with the joined R⁷R⁸ group being —CH═CHCH═CH—); and

R¹⁰ and R¹¹ may be joined to form a ring (such as a five-membered ring with the joined R¹⁰R¹¹ group being —CH₂CH₂—, a six-membered ring with the joined R¹⁰R¹¹ group being —CH₂CH₂CH_(2—)).

In some embodiments of Formulas (VIII), (IX), and (X), R⁴, R⁵, and R⁶ are independently selected from the group including hydrogen, hydrocarbyls, substituted hydrocarbyls, alkoxy, aryloxy, halogen, amino, and silyl, and where adjacent R groups (R⁴ and R⁵ and/or R⁵ and R⁶) are joined to form a substituted hydrocarbyl, unsubstituted hydrocarbyl, unsubstituted heterocyclic ring or substituted heterocyclic ring, where the ring has 5, 6, 7, or 8 ring atoms and where substitutions on the ring can join to form additional rings.

In some embodiments of Formulas (VIII), (IX), and (X), R⁷, R⁸, R⁹, and R¹⁹ are independently selected from the group including hydrogen, hydrocarbyls, substituted hydrocarbyls, alkoxy, halogen, amino, and silyl, and where adjacent R groups (R⁷ and R⁸ and/or R⁹ and R¹⁹) may be joined to form a saturated, substituted hydrocarbyl, unsubstituted hydrocarbyl, unsubstituted heterocyclic ring or substituted heterocyclic ring, where the ring has 5, 6, 7, or 8 ring carbon atoms and where substitutions on the ring can join to form additional rings.

In some embodiments of Formulas (VIII), (IX), and (X), R² and R³ are each, independently, selected from the group including hydrogen, hydrocarbyls, and substituted hydrocarbyls, alkoxy, silyl, amino, aryloxy, halogen, and phosphino, R² and R³ may be joined to form a saturated, substituted or unsubstituted hydrocarbyl ring, where the ring has 4, 5, 6, or 7 ring carbon atoms and where substitutions on the ring can join to form additional rings, or R² and R³ may be joined to form a saturated heterocyclic ring, or a saturated substituted heterocyclic ring where substitutions on the ring can join to form additional rings.

In some embodiments of Formulas (VIII), (IX), and (X), R¹¹ and R¹² are each, independently, selected from the group including hydrogen, hydrocarbyls, and substituted hydrocarbyls, alkoxy, silyl, amino, aryloxy, halogen, and phosphino, R¹¹ and R¹² may be joined to form a saturated, substituted or unsubstituted hydrocarbyl ring, where the ring has 4, 5, 6, or 7 ring carbon atoms and where substitutions on the ring can join to form additional rings, or R¹¹ and R¹² may be joined to form a saturated heterocyclic ring, or a saturated substituted heterocyclic ring where substitutions on the ring can join to form additional rings, or R¹¹ and R¹⁰ may be joined to form a saturated heterocyclic ring, or a saturated substituted heterocyclic ring where substitutions on the ring can join to form additional rings.

In some embodiments of Formulas (VIII), (IX), and (X), R¹ and R¹³ are independently selected from phenyl groups that are variously substituted with from zero to five substituents that include F, Cl, Br, I, CF₃, NO₂, alkoxy, dialkylamino, aryl, and alkyl groups having 1 to 10 carbons, such as methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, nonyl, decyl, and isomers thereof.

In at least one embodiment of Formula (IX), suitable R¹²-E-R¹¹ groups include CH₂, CMe₂, SiMe₂, SiEt₂, SiPr₂, SiBu₂, SiPh₂, Si(aryl)₂, Si(alkyl)₂, CH(aryl), CH(Ph), CH(alkyl), and CH(2-isopropylphenyl), where alkyl is a C₁ to C₄₀ alkyl group (such as C₁ to C₂₀ alkyl, such as one or more of methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, nonyl, decyl, undecyl, dodecyl, and isomers thereof), aryl is a C₅ to C₄₀ aryl group (such as a C₆ to C₂₀ aryl group, such as phenyl or substituted phenyl, such as phenyl, 2-isopropylphenyl, or 2-tertbutylphenyl).

In at least one embodiment of Formula (X), R¹¹, R¹², R⁹, R¹⁴, and R¹⁰ are independently selected from the group consisting of hydrogen, hydrocarbyls, substituted hydrocarbyls, alkoxy, halogen, amino, and silyl, and where adjacent R groups (R¹⁰ and R¹⁴, and/or R¹¹ and R¹⁴, and/or R⁹ and R¹⁰) may be joined to form a saturated, substituted hydrocarbyl, unsubstituted hydrocarbyl, unsubstituted heterocyclic ring or substituted heterocyclic ring, where the ring has 5, 6, 7, or 8 ring carbon atoms and where substitutions on the ring can join to form additional rings.

In some embodiments of Formulas (VIII), (IX), and (X), the R groups (i.e., one or more of R² to R¹⁴) and other R groups mentioned hereafter may contain from 1 to 30, such as 2 to 20 carbon atoms, such as from 6 to 20 carbon atoms. In some embodiments of Formulas (VIII), (IX), and (X), the R groups e (i.e., one or more of R² to R¹⁴) and other R groups mentioned hereafter, may be independently selected from the group including hydrogen, methyl, ethyl, phenyl, isopropyl, isobutyl, trimethylsilyl, and —CH₂—Si(Me)₃.

In some embodiments of formulas (VIII), (IX), and (X), the quinolinyldiamide complex is linked to one or more additional transition metal complex, such as a quinolinyldiamide complex or another suitable non-metallocene, through an R group in such a fashion as to make a bimetallic, trimetallic, or multimetallic complex that may be used as a catalyst component for olefin polymerization. The linker R-group in such a complex may contain 1 to 30 carbon atoms.

In some embodiments of Formulas (VIII), (IX), and (X), E is carbon and R¹¹ and R¹² are independently selected from phenyl groups that are substituted with 0, 1, 2, 3, 4, or 5 substituents selected from the group consisting of F, Cl, Br, I, CF₃, NO₂, alkoxy, dialkylamino, hydrocarbyl, and substituted hydrocarbyl groups with from one to ten carbons.

In at least one embodiment of Formulas (IX) or (X), R¹¹ and R¹² are independently selected from hydrogen, methyl, ethyl, phenyl, isopropyl, isobutyl, —CH₂—Si(Me)₃, and trimethylsilyl.

In at least one embodiment of Formulas (IX), and (X), R⁷, R⁸, R⁹, and R¹⁰ are independently selected from hydrogen, methyl, ethyl, propyl, isopropyl, phenyl, cyclohexyl, fluoro, chloro, methoxy, ethoxy, phenoxy, —CH₂—Si(Me)₃, and trimethylsilyl.

In some embodiments of Formulas (VIII), (IX), and (X), R², R³, R⁴, R⁵, and R⁶ are independently selected from the group consisting of hydrogen, hydrocarbyls, alkoxy, silyl, amino, substituted hydrocarbyls, and halogen.

In at least one embodiment of Formula (X), R¹⁰, R¹¹ and R¹⁴ are independently selected from hydrogen, methyl, ethyl, phenyl, isopropyl, isobutyl, —CH₂—Si(Me)₃, and trimethylsilyl.

In some embodiments of Formulas (VIII), (IX), and (X), each L is independently selected from Et₂O, MeOtBu, Et₃N, PhNMe₂, MePh₂N, tetrahydrofuran, and dimethylsulfide.

In some embodiments of Formulas (VIII), (IX), and (X), each X is independently selected from methyl, benzyl, trimethylsilyl, neopentyl, ethyl, propyl, butyl, phenyl, hydrido, chloro, fluoro, bromo, iodo, dimethylamido, diethylamido, dipropylamido, and diisopropylamido.

In some embodiments of Formulas (VIII), (IX), and (X), R¹ is 2,6-diisopropylphenyl, 2,4,6-triisopropylphenyl, 2,6-diisopropyl-4-methylphenyl, 2,6-diethylphenyl, 2-ethyl-6-isopropylphenyl, 2,6-bis(3-pentyl)phenyl, 2,6-dicyclopentylphenyl, or 2,6-dicyclohexylphenyl.

In some embodiments of Formulas (VIII), (IX), and (X), R¹³ is phenyl, 2-methylphenyl, 2-ethylphenyl, 2-propylphenyl, 2,6-dimethylphenyl, 2-isopropylphenyl, 4-methylphenyl, 3,5-dimethylphenyl, 3,5-di-tert-butylphenyl, 4-fluorophenyl, 3-methylphenyl, 4-dimethylaminophenyl, or 2-phenylphenyl.

In at least one embodiment of Formula (IX), J is dihydro-1H-indenyl and R¹ is 2,6-dialkylphenyl or 2,4,6-trialkylphenyl.

In some embodiments of Formulas (VIII), (IX), and (X), R¹ is 2,6-diisopropylphenyl and R¹³ is a hydrocarbyl group containing 1, 2, 3, 4, 5, 6, or 7 carbon atoms.

An exemplary catalyst used for polymerizations of the present disclosure is (QDA-1)HfMe₂, as described in US Pub. No. 2018/0002352 A1.

In at least one embodiment, the catalyst compound is a bis(phenolate) catalyst compound represented by Formula (XI):

where:

M is a Group 4 metal, such as Hf or Zr. X¹ and X² are independently a univalent C₁-C₂₀ hydrocarbyl, C₁-C₂₀ substituted hydrocarbyl, a heteroatom or a heteroatom-containing group, or X¹ and X² join together to form a C₄-C₆₂ cyclic or polycyclic ring structure. R¹, R², R³, R⁴, R⁵, R⁶, R⁷, R⁸, R⁹, and R¹⁰ is independently hydrogen, C₁-C₄₀ hydrocarbyl, C₁-C₄₀ substituted hydrocarbyl, a heteroatom or a heteroatom-containing group, or two or more of R¹, R², R³, R⁴, R⁵, R⁶, R⁷, R⁸, R⁹, or R¹⁰ are joined together to form a C₄-C₆₂ cyclic or polycyclic ring structure, or a combination thereof; Q is a neutral donor group; J is heterocycle, a substituted or unsubstituted C₇-C₆₀ fused polycyclic group, where at least one ring is aromatic and where at least one ring, which may or may not be aromatic, has at least five ring atoms' G is as defined for J or may be hydrogen, C₂-C₆₀ hydrocarbyl, C₁-C₆₀ substituted hydrocarbyl, or may independently form a C₄-C₆₀ cyclic or polycyclic ring structure with R⁶, R⁷, or R⁸ or a combination thereof; Y is divalent C₁-C₂₀ hydrocarbyl or divalent C₁-C₂₀ substituted hydrocarbyl or (-Q-Y—) together form a heterocycle; and heterocycle may be aromatic and/or may have multiple fused rings.

In at least one embodiment, the catalyst compound represented by Formula (XI) is represented by Formula (XII) or Formula (XIII):

M is Hf, Zr, or Ti. X¹, X², R¹, R², R³, R⁴, R⁵, R⁶, R⁷, R⁸, R⁹, R¹⁰, and Y are as defined for Formula (XI). R¹¹, R¹², R¹³, R¹⁴, R¹⁵, R¹⁶, R¹⁷, R¹⁸, R¹⁹, R²⁰, R²¹, R²², R²³, R²⁴, R²⁵, R²⁶, R²⁷, and R²⁸ is independently a hydrogen, C₁-C₄₀ hydrocarbyl, C₁-C₄₀ substituted hydrocarbyl, a functional group including elements from Groups 13 to 17, or two or more of R¹, R², R³, R⁴, R⁵, R⁶, R⁷, R⁸, R⁹, R¹⁰R¹¹, R¹², R¹³, R¹⁴, R¹⁵, R¹⁶, R¹⁷, R¹⁸, R¹⁹, R²⁰, R²¹, R²², R²³, R²⁴, R²⁵, R²⁶, R²⁷, and R²⁸ may independently join together to form a C₄-C₆₂ cyclic or polycyclic ring structure, or a combination thereof; R¹¹ and R¹² may join together to form a five- to eight-membered heterocycle; Q* is a group 15 or 16 atom; z is 0 or 1; J* is CR″ or N, and G* is CR″ or N, where R″ is C₁-C₂₀ hydrocarbyl or carbonyl-containing C₁-C₂₀ hydrocarbyl; and z=0 if Q* is a group 16 atom, and z=1 if Q* is a group 15 atom.

In at least one embodiment the catalyst is an iron complex represented by Formula (XIV):

where:

A is chlorine, bromine, iodine, —CF₃ or —OR¹¹;

each of R¹ and R² is independently hydrogen, C₁-C₂₂-alkyl, C₂-C₂₂-alkenyl, C₆-C₂₂-aryl, arylalkyl where alkyl has from 1 to 10 carbon atoms and aryl has from 6 to 20 carbon atoms, or five-, six- or seven-membered heterocyclyl including at least one atom selected from the group consisting of N, P, O and S;

where each of R¹ and R² is optionally substituted by halogen, —NR¹¹ ₂, —OR¹¹ or —SiR¹² ₃;

where R¹ optionally bonds with R³, and R² optionally bonds with R⁵, in each case to independently form a five-, six- or seven-membered ring;

R⁷ is a C₁-C₂₀ alkyl;

each of R³, R⁴, R⁵, R⁸, R⁹, R¹⁰, R¹⁵, R¹⁶, and R¹⁷ is independently hydrogen, C₁-C₂₂-alkyl, C₂-C₂₂-alkenyl, C₆-C₂₂-aryl, arylalkyl where alkyl has from 1 to 10 carbon atoms and aryl has from 6 to 20 carbon atoms, —NR¹¹ ₂, —OR¹¹, halogen, —SiR¹² ₃ or five-, six- or seven-membered heterocyclyl including at least one atom selected from the group consisting of N, P, O, and S;

where R³, R⁴, R⁵, R⁷, R⁸, R⁹, R¹⁰, R¹⁵, R¹⁶, and R¹⁷ are optionally substituted by halogen, —NR¹¹ ₂, —OR¹¹ or —SiR¹² ₃;

where R³ optionally bonds with R⁴, R⁴ optionally bonds with R⁵, R⁷ optionally bonds with R¹⁰, R¹⁰ optionally bonds with R⁹, R⁹ optionally bonds with R⁸, R¹⁷ optionally bonds with R¹⁶, and R¹⁶ optionally bonds with R¹⁵, in each case to independently form a five-, six- or seven-membered carbocyclic or heterocyclic ring, the heterocyclic ring including at least one atom from the group consisting of N, P, O and S;

R¹³ is C₁-C₂O-alkyl bonded with the aryl ring via a primary or secondary carbon atom;

R¹⁴ is chlorine, bromine, iodine, —CF₃ or —OR¹¹, or C₁-C₂₀-alkyl bonded with the aryl ring;

each R¹¹ is independently hydrogen, C₁-C₂₂-alkyl, C₂-C₂₂-alkenyl, C₆-C₂₂-aryl, arylalkyl where alkyl has from 1 to 10 carbon atoms and aryl has from 6 to 20 carbon atoms, or —SiR¹² ₃, where R¹¹ is optionally substituted by halogen, or two R¹¹ radicals optionally bond to form a five- or six-membered ring;

each R¹² is independently hydrogen, C₁-C₂₂-alkyl, C₂-C₂₂-alkenyl, C₆-C₂₂-aryl, arylalkyl where alkyl has from 1 to 10 carbon atoms and aryl has from 6 to 20 carbon atoms, or two R¹² radicals optionally bond to form a five- or six-membered ring;

each of E¹, E², and E³ is independently carbon, nitrogen or phosphorus;

each u is independently 0 if E¹, E², and E³ is nitrogen or phosphorus and is 1 if E¹, E², and E³ is carbon;

each X is independently fluorine, chlorine, bromine, iodine, hydrogen, C₁-C₂₀-alkyl, C₂-C₁₀-alkenyl, C₆-C₂₀-aryl, arylalkyl where alkyl has from 1 to 10 carbon atoms and aryl has from 6 to 20 carbon atoms, —NR¹⁸ ₂, OR¹⁸, SR¹⁸, —SO₃R¹⁸, —OC(O)R¹⁸, —CN, —SCN, β-diketonate, —CO, —BF₄ ⁻, —PF₆ ⁻ or bulky non-coordinating anions, and the radicals X can be bonded with one another;

each R¹⁸ is independently hydrogen, C₁-C₂₀-alkyl, C₂-C₂₀-alkenyl, C₆-C₂₀-aryl, arylalkyl where alkyl has from 1 to 10 carbon atoms and aryl has from 6 to 20 carbon atoms, or —SiR¹⁹ ₃, where R¹⁸ can be substituted by halogen or nitrogen- or oxygen-containing groups and two R¹⁸ radicals optionally bond to form a five- or six-membered ring;

each R¹⁹ is independently hydrogen, C₁-C₂₀-alkyl, C₂-C₂₀-alkenyl, C₆-C₂₀-aryl or arylalkyl where alkyl has from 1 to 10 carbon atoms and aryl has from 6 to 20 carbon atoms, where R¹⁹ can be substituted by halogen or nitrogen- or oxygen-containing groups or two R¹⁹ radicals optionally bond to form a five- or six-membered ring;

s is 1, 2, or 3;

D is a neutral donor; and

t is 0 to 2.

In another embodiment, the catalyst is a phenoxyimine compound represented by the Formula (XV):

where M represents a transition metal atom selected from the groups 3 to 11 metals in the periodic table; k is an integer of 1 to 6; m is an integer of 1 to 6; R^(a) to R^(f) may be the same or different from one another and each represent a hydrogen atom, a halogen atom, a hydrocarbon group, a heterocyclic compound residue, an oxygen-containing group, a nitrogen-containing group, a boron-containing group, a sulfur-containing group, a phosphorus-containing group, a silicon-containing group, a germanium-containing group or a tin-containing group, among which 2 or more groups may be bound to each other to form a ring; when k is 2 or more, R^(a) groups, R^(b) groups, R^(c) groups, R^(d) groups, R^(e) groups, or R^(f) groups may be the same or different from one another, one group of R^(a) to R^(f) contained in one ligand and one group of R^(a) to R^(f) contained in another ligand may form a linking group or a single bond, and a heteroatom contained in R^(a) to R^(f) may coordinate with or bind to M; m is a number satisfying the valence of M; Y represents a hydrogen atom, a halogen atom, an oxygen atom, a hydrocarbon group, an oxygen-containing group, a sulfur-containing group, a nitrogen-containing group, a boron-containing group, an aluminum-containing group, a phosphorus-containing group, a halogen-containing group, a heterocyclic compound residue, a silicon-containing group, a germanium-containing group or a tin-containing group; when m is 2 or more, a plurality of groups represented by Y may be the same or different from one another, and a plurality of groups represented by Y may be mutually bound to form a ring.

In another embodiment, the catalyst is a bis(imino)pyridyl of the Formula (XVI):

where:

M is Co or Fe; each X is an anion; n is 1, 2 or 3, so that the total number of negative charges on said anion or anions is equal to the oxidation state of a Fe or Co atom present in Formula (XVI);

R¹, R² and R³ are each independently hydrogen, hydrocarbyl, substituted hydrocarbyl, or an inert functional group;

R⁴ and R⁵ are each independently hydrogen, hydrocarbyl, an inert functional group or substituted hydrocarbyl;

R⁶ is Formula (XVII):

and R⁷ is Formula (XVIII):

R⁸ and R¹³ are each independently hydrocarbyl, substituted hydrocarbyl or an inert functional group;

R⁹, R¹⁰, R¹¹, R¹⁴, R¹⁵ and R¹⁶ are each independently hydrogen, hydrocarbyl, substituted hydrocarbyl or an inert functional group;

R¹² and R¹⁷ are each independently hydrogen, hydrocarbyl, substituted hydrocarbyl or an inert functional group;

and provided that two of R⁸, R⁹, R¹⁰, R¹¹, R¹², R¹³, R¹⁴, R¹⁵, R¹⁶ and R¹⁷ that are adjacent to one another, together may form a ring.

In at least one embodiment, the catalyst compound is represented by the Formula (XIX):

where M¹ is selected from the group consisting of titanium, zirconium, hafnium, vanadium, niobium, tantalum, chromium, molybdenum and tungsten. In at least one embodiment of Formula (XIX), M¹ is zirconium.

In some embodiments of Formula (XIX), each of Q¹, Q², Q³, and Q⁴ is independently oxygen or sulfur. In some embodiments of Formula (XIX), at least one of Q¹, Q², Q³, and Q⁴ is oxygen, alternately all of Q¹, Q², Q³, and Q⁴ are oxygen.

In some embodiments of Formula (XIX), R¹ and R² are independently hydrogen, halogen, hydroxyl, hydrocarbyl, or substituted hydrocarbyl (such as C₁-C₁₀ alkyl, C₁-C₁₀ alkoxy, C₆-C₂₀ aryl, C₆-C₁₀ aryloxy, C₂-C₁₀ alkenyl, C₂-C₄₀ alkenyl, C₇-C₄₀ arylalkyl, C₇-C₄₀ alkylaryl, C₈-C₄₀ arylalkenyl, or conjugated diene which is optionally substituted with one or more hydrocarbyl, tri(hydrocarbyl) silyl or tri(hydrocarbyl) silylhydrocarbyl, the diene having up to 30 atoms other than hydrogen). In some embodiments of Formula (XIX), R¹ and R² can be a halogen selected from fluorine, chlorine, bromine, or iodine. In some embodiments of Formula (XIX), R¹ and R² are chlorine.

Alternatively, in some embodiments of Formula (XIX), R¹ and R² may also be joined together to form an alkanediyl group or a conjugated C₄-C₄₀ diene ligand which is coordinated to M¹. In some embodiments of Formula (XIX), R¹ and R² may be identical or different conjugated dienes, optionally substituted with one or more hydrocarbyl, tri(hydrocarbyl) silyl or tri(hydrocarbyl) silylhydrocarbyl, the dienes having up to 30 atoms not counting hydrogen and/or forming a π-complex with M¹.

Exemplary groups suitable for R¹ and or R² of Formula (XIX) can include 1,4-diphenyl, 1,3-butadiene, 1,3-pentadiene, 2-methyl 1,3-pentadiene, 2,4-hexadiene, 1-phenyl, 1,3-pentadiene, 1,4-dibenzyl, 1,3-butadiene, 1,4-ditolyl-1,3-butadiene, 1,4-bis (trimethylsilyl)-1,3-butadiene, and 1,4-dinaphthalenyl-1,3-butadiene. R¹ and R² can be identical and are C₁-C₃ alkyl or alkoxy, C₆-C₁₀ aryl or aryloxy, C₂-C₄ alkenyl, C₇-C₁₀ arylalkyl, C₇-C₁₂ alkylaryl, or halogen.

In some embodiments of Formula (XIX), each of R⁴, R⁵, R⁶, R⁷, R⁸, R⁹, R¹⁰, R¹¹, R¹², R¹³, R¹⁴, R¹⁵, R¹⁶, R¹⁷, R¹⁸, and R¹⁹ is independently hydrogen, halogen, C₁-C₄₀ hydrocarbyl or C₁-C₄₀ substituted hydrocarbyl (such as C₁-C₁₀ alkyl, C₁-C₁₀ alkoxy, C₆-C₂₀ aryl, C₆-C₁₀ aryloxy, C₂-C₁₀ alkenyl, C₂-C₄₀ alkenyl, C₇-C₄₀ arylalkyl, C₇-C₄₀ alkylaryl, C₈-C₄₀ arylalkenyl, or conjugated diene which is optionally substituted with one or more hydrocarbyl, tri(hydrocarbyl) silyl or tri(hydrocarbyl) silylhydrocarbyl, the diene having up to 30 atoms other than hydrogen), —NR′₂, —SR′, —OR, —OSiR′₃, —PR′₂, where each R′ is hydrogen, halogen, C₁-C₁₀ alkyl, or C₆-C₁₀ aryl, or one or more of R⁴ and R⁵, R⁵ and R⁶, R⁶ and R⁷, R⁸ and R⁹, R⁹ and R¹⁰, R¹⁰ and R¹¹, R¹² and R¹³, R¹³ and R¹⁴, R¹⁴ and R¹⁵, R¹⁶ and R¹⁷, R¹⁷ and R¹⁸, and R¹⁸ and R¹⁹ are joined to form a saturated ring, unsaturated ring, substituted saturated ring, or substituted unsaturated ring. In some embodiments of Formula (XIX), C₁-C₄₀ hydrocarbyl is selected from methyl, ethyl, propyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, n-pentyl, isopentyl, sec-pentyl, n-hexyl, isohexyl, sec-hexyl, n-heptyl, isoheptyl, sec-heptyl, n-octyl, isooctyl, sec-octyl, n-nonyl, isononyl, sec-nonyl, n-decyl, isodecyl, and sec-decyl. In some embodiments of Formula (XIX), R¹¹ and R¹² are C₆-C₁₀ aryl such as phenyl or naphthalenyl optionally substituted with C₁-C₄₀ hydrocarbyl, such as C₁-C₁₀ hydrocarbyl. In some embodiments of Formula (XIX), R⁶ and R¹⁷ are C₁₋₄₀ alkyl, such as C₁-C₁₀ alkyl.

In some embodiments of Formula (XIX), each of R⁴, R⁵, R⁶, R⁷, R⁸, R⁹, R¹⁰, R¹³, R¹⁴, R¹⁵, R¹⁶, R¹⁷, R¹⁸, and R¹⁹ is independently hydrogen or C₁-C₄₀ hydrocarbyl. In at least one embodiment, C₁-C₄₀ hydrocarbyl is selected from methyl, ethyl, propyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, n-pentyl, isopentyl, sec-pentyl, n-hexyl, isohexyl, sec-hexyl, n-heptyl, isoheptyl, sec-heptyl, n-octyl, isooctyl, sec-octyl, n-nonyl, isononyl, sec-nonyl, n-decyl, isodecyl, and sec-decyl. In some embodiments of Formula (XIX), each of R⁶ and R¹⁷ is C₁-C₄₀ hydrocarbyl and R⁴, R⁵, R⁷, R⁸, R⁹, R¹⁰, R¹³, R¹⁴, R¹⁵, R¹⁶, R¹⁸, and R¹⁹ is hydrogen. In some embodiments of Formula (XIX), C₁-C₄₀ hydrocarbyl is selected from methyl, ethyl, propyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, n-pentyl, isopentyl, sec-pentyl, n-hexyl, isohexyl, sec-hexyl, n-heptyl, isoheptyl, sec-heptyl, n-octyl, isooctyl, sec-octyl, n-nonyl, isononyl, sec-nonyl, n-decyl, isodecyl, and sec-decyl.

In some embodiments of Formula (XIX), R³ is a C₁-C₄₀ unsaturated alkyl or substituted C₁-C₄₀ unsaturated alkyl (such as C₁-C₁₀ alkyl, C₁-C₁₀ alkoxy, C₆-C₂₀ aryl, C₆-C₁₀ aryloxy, C₂-C₁₀ alkenyl, C₂-C₄₀ alkenyl, C₇-C₄₀ arylalkyl, C₇-C₄₀ alkylaryl, C₈-C₄₀ arylalkenyl, or conjugated diene which is optionally substituted with one or more hydrocarbyl, tri(hydrocarbyl) silyl or tri(hydrocarbyl) silylhydrocarbyl, the diene having up to 30 atoms other than hydrogen).

In some embodiments of Formula (XIX), R³ is a hydrocarbyl including a vinyl moiety. “Vinyl” and “vinyl moiety” are used interchangeably and include a terminal alkene, e.g., represented by the structure

Hydrocarbyl of R³ may be further substituted (such as C₁-C₁₀ alkyl, C₁-C₁₀ alkoxy, C₆-C₂₀ aryl, C₆-C₁₀ aryloxy, C₂-C₁₀ alkenyl, C₂-C₄₀ alkenyl, C₇-C₄₀ arylalkyl, C₇-C₄₀ alkylaryl, C₈-C₄₀ arylalkenyl, or conjugated diene which is optionally substituted with one or more hydrocarbyl, tri(hydrocarbyl) silyl or tri(hydrocarbyl) silylhydrocarbyl, the diene having up to 30 atoms other than hydrogen). In some embodiments of Formula (XIX), R³ is C₁-C₄₀ unsaturated alkyl that is vinyl or substituted C₁-C₄₀ unsaturated alkyl that is vinyl. R³ can be represented by the structure —R′CH═CH₂ where R′ is C₁-C₄₀ hydrocarbyl or C₁-C₄₀ substituted hydrocarbyl (such as C₁-C₁₀ alkyl, C₁-C₁₀ alkoxy, C₆-C₂₀ aryl, C₆-C₁₀ aryloxy, C₂-C₁₀ alkenyl, C₂-C₄₀ alkenyl, C₇-C₄₀ arylalkyl, C₇-C₄₀ alkylaryl, C₈-C₄₀ arylalkenyl, or conjugated diene which is optionally substituted with one or more hydrocarbyl, tri(hydrocarbyl) silyl or tri(hydrocarbyl) silylhydrocarbyl, the diene having up to 30 atoms other than hydrogen). In some embodiments of Formula (XIX), C₁-C₄₀ hydrocarbyl is selected from methyl, ethyl, propyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, n-pentyl, isopentyl, sec-pentyl, n-hexyl, isohexyl, sec-hexyl, n-heptyl, isoheptyl, sec-heptyl, n-octyl, isooctyl, sec-octyl, n-nonyl, isononyl, sec-nonyl, n-decyl, isodecyl, and sec-decyl.

In some embodiments of Formula (XIX), R³ is 1-propenyl, 1-butenyl, 1-pentenyl, 1-hexenyl, 1-heptenyl, 1-octenyl, 1-nonenyl, or 1-decenyl.

In some embodiments, the catalyst is a Group 15-containing metal compound represented by Formulas (XX) or (XXI):

where M is a Group 3 to 12 transition metal or a Group 13 or 14 main group metal, a Group 4, 5, or 6 metal. In some embodiments, M is a Group 4 metal, such as zirconium, titanium, or hafnium. Each X is independently a leaving group, such as an anionic leaving group. The leaving group may include a hydrogen, a hydrocarbyl group, a heteroatom, a halogen, or an alkyl; y is 0 or 1 (when y is 0 group L′ is absent). The term ‘n’ is the oxidation state of M. In various embodiments of Formulas (XX) and (XXI), n is +3, +4, or +5. In some embodiments, n is +4. The term ‘m’ represents the formal charge of the YZL or the YZL′ ligand, and is 0, −1, −2 or −3 in various embodiments. In some embodiments of Formulas (XX) and (XXI), m is −2. L is a Group 15 or 16 element, such as nitrogen or oxygen; L′ is a Group 15 or 16 element or Group 14 containing group, such as carbon, silicon or germanium. Y is a Group 15 element, such as nitrogen or phosphorus. In some embodiments of Formulas (XX) and (XXI), Y is nitrogen. Z is a Group 15 element, such as nitrogen or phosphorus. In some embodiments of Formulas (XX) and (XXI), Z is nitrogen. R¹ and R² are, independently, a C₁ to C₂₀ hydrocarbon group, a heteroatom containing group having up to twenty carbon atoms, silicon, germanium, tin, lead, or phosphorus. In some embodiments of Formulas (XX) and (XXI), R¹ and R² are a C₂ to C₂₀ alkyl, aryl or aralkyl group, such as a C₂ to C₂₀ linear, branched or cyclic alkyl group, or a C₂ to C₂₀ hydrocarbon group. R¹ and R² may also be interconnected to each other. R³ may be absent or may be a hydrocarbon group, a hydrogen, a halogen, a heteroatom containing group. In some embodiments of Formulas (XX) and (XXI), R³ is absent, for example, if L is an oxygen, or a hydrogen, or a linear, cyclic, or branched alkyl group having 1 to 20 carbon atoms. R⁴ and R⁵ are independently an alkyl group, an aryl group, substituted aryl group, a cyclic alkyl group, a substituted cyclic alkyl group, a cyclic aralkyl group, a substituted cyclic aralkyl group, or multiple ring system, often having up to 20 carbon atoms. In some embodiments of Formulas (XX) and (XXI), R⁴ and R⁵ have from 3 to 10 carbon atoms, or are a C₁ to C₂₀ hydrocarbon group, a C₁ to C₂₀ aryl group or a C₁ to C₂₀ aralkyl group, or a heteroatom containing group. R⁴ and R⁵ may be interconnected to each other. R⁶ and R⁷ are independently absent, hydrogen, an alkyl group, halogen, heteroatom, or a hydrocarbyl group, such as a linear, cyclic or branched alkyl group having 1 to 20 carbon atoms. In some embodiments of Formulas (XX) and (XXI), R⁶ and R⁷ are absent. R* may be absent, or may be a hydrogen, a Group 14 atom containing group, a halogen, or a heteroatom containing group.

“Formal charge of the YZL or YZL′ ligand” means the charge of the entire ligand absent the metal and the leaving groups X. “R¹ and R² may also be interconnected” means that R¹ and R² may be directly bound to each other or may be bound to each other through other groups. “R⁴ and R⁵ may also be interconnected” means that R⁴ and R⁵ may be directly bound to each other or may be bound to each other through other groups. An alkyl group may be linear, branched alkyl radicals, alkenyl radicals, alkynyl radicals, cycloalkyl radicals, aryl radicals, acyl radicals, aroyl radicals, alkoxy radicals, aryloxy radicals, alkylthio radicals, dialkylamino radicals, alkoxycarbonyl radicals, aryloxycarbonyl radicals, carbomoyl radicals, alkyl- or dialkyl-carbamoyl radicals, acyloxy radicals, acylamino radicals, aroylamino radicals, straight, branched or cyclic, alkylene radicals, or combination thereof. An aralkyl group is defined to be a substituted aryl group.

In one or more embodiments, R⁴ and R⁵ are independently a group represented by Structure (XXII):

where R⁸ to R¹² are each independently hydrogen, a C₁ to C₄₀ alkyl group, a halide, a heteroatom, a heteroatom containing group containing up to 40 carbon atoms. In some embodiments, R⁸ to R¹² are a C₁ to C₂₀ linear or branched alkyl group, such as a methyl, ethyl, propyl, or butyl group. Two of the R groups may form a cyclic group and/or a heterocyclic group. The cyclic groups may be aromatic. In one embodiment R⁹, R¹⁰ and R¹² are independently a methyl, ethyl, propyl, or butyl group (including all isomers). In another embodiment, R⁹, R¹⁰ and R¹² are methyl groups, and R⁸ and R¹¹ are hydrogen.

In one or more embodiments, R⁴ and R⁵ are both a group represented by Structure (XXIII):

where M is a Group 4 metal, such as zirconium, titanium, or hafnium. In at least one embodiment, M is zirconium. Each of L, Y, and Z may be a nitrogen. Each of R¹ and R² may be —CH₂—CH₂—. R³ may be hydrogen, and R⁶ and R⁷ may be absent.

In some embodiments, the catalyst compounds described in PCT/US2018/051345, filed Sep. 17, 2018 may be used with the activators described, such as the catalyst compounds described at Page 16 to Page 32 of the application as filed.

In some embodiments, a co-activator is combined with the catalyst compound (such as halogenated catalyst compounds described above) to form an alkylated catalyst compound. Organoaluminum compounds which may be utilized as co-activators include, for example, trialkyl aluminum compounds, such as trimethylaluminum, triethylaluminum, triisobutylaluminum, tri-n-hexylaluminum, tri-n-octylaluminum, and the like, or alumoxanes.

In some embodiments, two or more different catalyst compounds are present in the catalyst system used. In some embodiments, two or more different catalyst compounds are present in the reaction zone where the process(es) described occur. When two transition metal compound based catalysts are used in one reactor as a mixed catalyst system, the two transition metal compounds may be chosen such that the two are compatible. A simple screening method such as by ¹H or ¹³C NMR, can be used to determine which transition metal compounds are compatible. The same activator may be used for the transition metal compounds, alternatively, two different activators may be used in combination. If one or more transition metal compounds contain an anionic ligand as a leaving group which is not a hydride, hydrocarbyl, or substituted hydrocarbyl, then the alumoxane or other alkyl aluminum is typically contacted with the transition metal compounds prior to addition of the non-coordinating anion activator.

The two transition metal compounds (pre-catalysts) may be used in any suitable ratio. Molar ratios of (A) transition metal compound to (B) transition metal compound (A:B) may include from about 1:1000 to about 1000:1, such as about 1:100 to about 500:1, about 1:10 to about 200:1, about 1:1 to about 100:1, and about 1:1 to about 75:1, and about 5:1 to about 50:1. The particular ratio chosen will depend on the exact pre-catalysts chosen, the method of activation, and the end product. In a particular embodiment, when using the two pre-catalysts, where both are activated with the same activator, useful mole percents, based upon the molecular weight of the pre-catalysts, are 10 to 99.9% A to 0.1 to 90% B, alternatively 25 to 99% A to 0.5 to 50% B, alternatively 50 to 99% A to 1 to 25% B, and alternatively 75 to 99% A to 1 to 10% B.

Polymer Processes

In some embodiments, the present disclosure provides polymerization processes where monomer (such as propylene or ethylene), and optionally comonomer, are contacted with a catalyst system including an activator and at least one catalyst compound, as described above. The catalyst compound and activator may be combined in any suitable order, and are combined typically prior to contacting with the monomer.

In at least one embodiment, a polymerization process includes a) contacting one or more olefin monomers with a catalyst system including: i) an activator and ii) a catalyst compound of the present disclosure. The activator is a non-coordination anion activator. The one or more olefin monomers may be propylene and/or ethylene and the polymerization process further includes heating the one or more olefin monomers and the catalyst system to 70° C. or more to form propylene polymers or ethylene polymers, such as propylene polymers.

Suitable monomers include substituted or unsubstituted C₂ to C₄₀ alpha olefins, such as C₂ to C₂₀ alpha olefins, such as C₂ to C₁₂ alpha olefins, such as ethylene, propylene, butene, pentene, hexene, heptene, octene, nonene, decene, undecene, dodecene and isomers thereof. In at least one embodiment, the monomer includes propylene and an optional comonomers including one or more propylene or C₄ to C₄₀ olefins, such as C₄ to C₂₀ olefins, such as C₆ to C₁₂ olefins. The C₄ to C₄₀ olefin monomers may be linear, branched, or cyclic. The C₄ to C₄₀ cyclic olefins may be strained or unstrained, monocyclic or polycyclic, and may optionally include heteroatoms and/or one or more functional groups. In at least one embodiment, the monomer includes propylene and an optional comonomers including one or more C₃ to C₄₀ olefins, such as C₄ to C₂₀ olefins, such as C₆ to C₁₂ olefins. The C₃ to C₄₀ olefin monomers may be linear, branched, or cyclic. The C₃ to C₄₀ cyclic olefins may be strained or unstrained, monocyclic or polycyclic, and may optionally include heteroatoms and/or one or more functional groups.

Exemplary C₂ to C₄₀ olefin monomers and optional comonomers include propylene, propylene, butene, pentene, hexene, heptene, octene, nonene, decene, undecene, dodecene, norbornene, norbornadiene, dicyclopentadiene, cyclopentene, cycloheptene, cyclooctene, cyclooctadiene, cyclododecene, 7-oxanorbornene, 7-oxanorbornadiene, substituted derivatives thereof, and isomers thereof, such as hexene, heptene, octene, nonene, decene, dodecene, cyclooctene, 1,5-cyclooctadiene, 1-hydroxy-4-cyclooctene, 1-acetoxy-4-cyclooctene, 5-methylcyclopentene, cyclopentene, dicyclopentadiene, norbornene, norbornadiene, and their respective homologs and derivatives, such as norbornene, norbornadiene, and dicyclopentadiene.

In at least one embodiment, one or more dienes are present in the polymer produced at up to 10 wt %, such as at 0.00001 to 1 wt %, such as 0.002 to 0.5 wt %, such as 0.003 to 0.2 wt %, based upon the total weight of the composition. In some embodiments, 500 ppm or less of diene is added to the polymerization, such as 400 ppm or less, such as 300 ppm or less. In other embodiments at least 50 ppm of diene is added to the polymerization, or 100 ppm or more, or 150 ppm or more.

Diene monomers include a hydrocarbon structure, such as C₄ to C₃₀, having at least two unsaturated bonds, where at least two of the unsaturated bonds are readily incorporated into a polymer by either a stereospecific or a non-stereospecific catalyst(s). The diene monomers can be selected from alpha, omega-diene monomers (i.e. di-vinyl monomers). The diolefin monomers are linear di-vinyl monomers, such as those containing from 4 to 30 carbon atoms. Examples of dienes include butadiene, pentadiene, hexadiene, heptadiene, octadiene, nonadiene, decadiene, undecadiene, dodecadiene, tridecadiene, tetradecadiene, pentadecadiene, hexadecadiene, heptadecadiene, octadecadiene, nonadecadiene, icosadiene, heneicosadiene, docosadiene, tricosadiene, tetracosadiene, pentacosadiene, hexacosadiene, heptacosadiene, octacosadiene, nonacosadiene, triacontadiene, 1,6-heptadiene, 1,7-octadiene, 1,8-nonadiene, 1,9-decadiene, 1,10-undecadiene, 1,11-dodecadiene, 1,12-tridecadiene, 1,13-tetradecadiene, and low molecular weight polybutadienes (Mw less than 1,000 g/mol). Cyclic dienes include cyclopentadiene, vinylnorbornene, norbornadiene, ethylidene norbornene, divinylbenzene, dicyclopentadiene or higher ring containing diolefins with or without substituents at various ring positions.

Polymerization processes of the present disclosure can be carried out in any suitable manner. Any suitable suspension, homogeneous, bulk, or solution phase polymerization process can be used. Such processes can be run in a batch, semi-batch, or continuous mode. Homogeneous polymerization processes can be performed. (A useful homogeneous polymerization process is one where at least 90 wt % of the product is soluble in the reaction media.) A bulk homogeneous process can be used. (An example bulk process is one where monomer concentration in all feeds to the reactor is 70 volume % or more.) Alternately, no solvent or diluent is present or added in the reaction medium, (except for the small amounts used as the carrier for the catalyst system or other additives, or amounts typically found with the monomer; e.g., propane in propylene).

Suitable diluents/solvents for polymerization include non-coordinating, inert liquids. Examples include straight and branched-chain hydrocarbons, such as isobutane, butane, pentane, isopentane, hexanes, isohexane, heptane, octane, dodecane, and mixtures thereof; cyclic and alicyclic hydrocarbons, such as cyclohexane, cycloheptane, methylcyclohexane, methylcycloheptane, and mixtures thereof, such as can be found commercially (Isopar™); perhalogenated hydrocarbons, such as perfluorinated C₄-C₁₀ alkanes, chlorobenzene, and aromatic and alkylsubstituted aromatic compounds, such as benzene, toluene, mesitylene, and xylene. Suitable solvents also include liquid olefins which may act as monomers or comonomers including ethylene, propylene, 1-butene, 1-hexene, 1-pentene, 3-methyl-1-pentene, 4-methyl-1-pentene, 1-octene, 1-decene, and mixtures thereof. In at least one embodiment, the solvent is not aromatic, such that aromatics are present in the solvent at less than 1 wt %, such as less than 0.5 wt %, such as less than 0 wt % based upon the weight of the solvents.

In at least one embodiment, the feed concentration of the monomers and comonomers for the polymerization is 60 vol % solvent or less, such as 40 vol % or less, such as 20 vol % or less, based on the total volume of the feedstream. The polymerization can be performed in a bulk process.

Polymerizations can be performed at any suitable temperature and/or pressure to obtain polymers, such as ethylene and or propylene polymers. Typical temperatures and/or pressures include a temperature of from about 0° C. to about 300° C., such as about 20° C. to about 200° C., such as about 35° C. to about 150° C., such as about 40° C. to about 120° C., such as about 45° C. to about 80° C., for example about 74° C., and at a pressure of from 0.35 MPa to 10 MPa, such as 0.45 MPa to 6 MPa, such as 0.5 MPa to 4 MPa.

In a typical polymerization, the run time of the reaction is up to 300 minutes, such as from about 5 to about 250 minutes, such as from about 10 to about 120 minutes.

In at least one embodiment, hydrogen is present in the polymerization reactor at a partial pressure of 0.001 to 50 psig (0.007 to 345 kPa), such as from 0.01 to 25 psig (0.07 to 172 kPa), such as 0.1 to 10 psig (0.7 to 70 kPa).

In at least one embodiment, the activity of the catalyst is from 50 gP/mmolCat/hour to 200,000 gP/mmolCat/hr, such as from 10,000 gP/mmolCat/hr to 150,000 gP/mmolCat/hr, such as from 40,000 gP/mmolCat/hr to 100,000 gP/mmolCat/hr, such as about 50,000 gP/mmolCat/hr or more, such as 70,000 gP/mmolCat/hr or more. In at least one embodiment, the conversion of olefin monomer is at least 10%, based upon polymer yield and the weight of the monomer entering the reaction zone, such as 20% or more, such as 30% or more, such as 50% or more, such as 80% or more.

In at least one embodiment, a catalyst system of the present disclosure is capable of producing a polyolefin. In at least one embodiment, a polyolefin is a homopolymer of ethylene or propylene or a copolymer of ethylene such as a copolymer of ethylene having from 0.1 to 25 wt % (such as from 0.5 to 20 wt %, such as from 1 to 15 wt %, such as from 5 to 17 wt %) of ethylene with the remainder balance being one or more C₃ to C₂₀ olefin comonomers (such as C₃ to C₁₂ alpha-olefin, such as propylene, butene, hexene, octene, decene, dodecene, such as propylene, butene, hexene, octene). A polyolefin can be a copolymer of propylene such as a copolymer of propylene having from 0.1 to 25 wt % (such as from 0.5 to 20 wt %, such as from 1 to 15 wt %, such as from 3 to 10 wt %) of propylene and from 99.9 to 75 wt % of one or more of C₂ or C₄ to C₂₀ olefin comonomer (such as ethylene or C₄ to C₁₂ alpha-olefin, such as butene, hexene, octene, decene, dodecene, such as ethylene, butene, hexene, octene).

In at least one embodiment, a catalyst system of the present disclosure is capable of producing polyolefins, such as polypropylene (e.g., iPP) or ethylene-octene copolymers, having an Mw from 40,000 to 1,500,000, such as from 70,000 to 1,000,000, such as from 90,000 to 500,000, such as from 90,000 to 250,000, such as from 90,000 to 200,000, such as from 90,000 to 110,000.

In at least one embodiment, a catalyst system of the present disclosure is capable of producing polyolefins, such as polypropylene (e.g., iPP) or ethylene-octene copolymers, having an Mn from 5,000 to 1,000,000, such as from 20,000 to 160,000, such as from 30,000 to 70,000, such as from 40,000 to 70,000. In at least one embodiment, a catalyst system of the present disclosure is capable of producing propylene polymers having an Mw/Mn value from 1 to 10, such as from 1.5 to 9, such as from 2 to 7, such as from 2 to 4, such as from 2.5 to 3, for example about 2.

In at least one embodiment, a catalyst system of the present disclosure is capable of producing polyolefins, such as polypropylene (e.g., iPP) or ethylene-octene, ethylene-propylene, or ethylene-butene copolymers, having a melting temperature (Tm) of less than 140° C., or 100° C. to 150° C., such as 110° C. to 140° C., such as 120° C. to 135° C., such as 130° C. to 135° C.

In at least one embodiment, little or no scavenger is used in the process to produce polymer, such as propylene polymer. Scavenger (such as trialkyl aluminum) can be present at zero mol %, alternately the scavenger is present at a molar ratio of scavenger metal to transition metal of less than 100:1, such as less than 50:1, such as less than 15:1, such as less than 10:1.

In at least one embodiment, the polymerization: 1) is conducted at temperatures of 0° C. to 300° C. (such as 25° C. to 150° C., such as 40° C. to 120° C., such as 70° C. to 110° C., such as 85° C. to 100° C.); 2) is conducted at a pressure of atmospheric pressure to 10 MPa (such as 0.35 to 10 MPa, such as from 0.45 to 6 MPa, such as from 0.5 to 4 MPa); 3) is conducted in an aliphatic hydrocarbon solvent (such as isobutane, butane, pentane, isopentane, hexanes, isohexane, heptane, octane, dodecane, and mixtures thereof; cyclic and alicyclic hydrocarbons, such as cyclohexane, cycloheptane, methylcyclohexane, methylcycloheptane, and mixtures thereof, where aromatics are present in the solvent at less than 1 wt %, such as less than 0.5 wt %, such as at 0 wt % based upon the weight of the solvents); and 4) the productivity of the catalyst compound is at least 30,000 gP/mmolCat/hr (such as at least 50,000 gP/mmolCat/hr, such as at least 60,000 gP/mmolCat/hr, such as at least 80,000 gP/mmolCat/hr, such as at least 100,000 gP/mmolCat/hr).

In at least one embodiment, the catalyst system used in the polymerization includes no more than one catalyst compound. A “reaction zone” also referred to as a “polymerization zone” is a vessel where polymerization takes place, for example a batch reactor. When multiple reactors are used in either series or parallel configuration, each reactor is considered as a separate polymerization zone. For a multi-stage polymerization in both a batch reactor and a continuous reactor, each polymerization stage is considered as a separate polymerization zone. In at least one embodiment, the polymerization occurs in one reaction zone.

Other additives may also be used in the polymerization, such as one or more scavengers, promoters, modifiers, chain transfer agents (such as diethyl zinc), hydrogen, or aluminum alkyls. Useful chain transfer agents are typically alkylalumoxanes, a compound represented by the formula AlR₃, ZnR₂ (where each R is, independently, a C₁-C₈ aliphatic radical, such as methyl, ethyl, propyl, butyl, phenyl, hexyl, octyl or an isomer thereof) or a combination thereof, such as diethyl zinc, methylalumoxane, trimethylaluminum, triisobutylaluminum, trioctylaluminum, or a combination thereof.

Solution Polymerization

A solution polymerization is a polymerization process in which the polymer is dissolved in a liquid polymerization medium, such as an inert solvent or monomer(s) or their blends. A solution polymerization is typically homogeneous. A homogeneous polymerization is one where the polymer product is dissolved in the polymerization medium. Such systems are typically not turbid as described in Oliveira, J. V. et al. (2000) “High-Pressure Phase Equilibria for Polypropylene-Hydrocarbon Systems,” Ind. Eng. Chem. Res., v.39, pp. 4627-4633. Typically solution polymerization involves polymerization in a continuous reactor in which the polymer formed and the starting monomer and catalyst materials supplied, are agitated to reduce or avoid concentration gradients and in which the monomer acts as a diluent or solvent or in which a hydrocarbon is used as a diluent or solvent. Suitable processes typically operate at temperatures from about 0° C. to about 250° C., such as about 10° C. to about 150° C., such as about 40° C. to about 140° C., such as about 50° C. to about 120° C., and at pressures of about 0.1 MPa or more, such as 2 MPa or more. The pressure typically can be about 200 MPa or less, such as 120 MPa or less. Temperature control in the reactor may be obtained by balancing the heat of polymerization and with reactor cooling by reactor jackets or cooling coils to cool the contents of the reactor, auto refrigeration, pre-chilled feeds, vaporization of liquid medium (diluent, monomers or solvent) or combinations of all three. Adiabatic reactors with pre-chilled feeds can also be used. The purity, type, and amount of solvent can be selected for improved catalyst productivity for a particular type of polymerization. The solvent can be also introduced as a catalyst carrier. The solvent can be introduced as a gas phase or as a liquid phase depending on the pressure and temperature. Advantageously, the solvent can be kept in the liquid phase and introduced as a liquid. Solvent can be introduced in the feed to the polymerization reactors.

Polyolefin Products

The present disclosure also provides compositions of matter which can be produced by methods described.

In at least one embodiment, a polyolefin is a propylene homopolymer, an ethylene homopolymer or an ethylene copolymer, such as propylene-ethylene and/or ethylene-alphaolefin (such as C₄ to C₂₀) copolymer (such as an ethylene-hexene copolymer or an ethylene-octene copolymer). A polyolefin can have an Mw/Mn of greater than 1 to 4 (such as greater than 1 to 3).

In at least one embodiment, a polyolefin is a homopolymer of ethylene or propylene or a copolymer of ethylene such as a copolymer of ethylene having from 0.1 to 25 wt % (such as from 0.5 to 20 wt %, such as from 1 to 15 wt %, such as from 5 to 17 wt %) of ethylene with the remainder balance being one or more C₃ to C₂₀ olefin comonomers (such as C₃ to C₁₂ alpha-olefin, such as propylene, butene, hexene, octene, decene, dodecene, such as propylene, butene, hexene, octene). A polyolefin can be a copolymer of propylene such as a copolymer of propylene having from 0.1 to 25 wt % (such as from 0.5 to 20 wt %, such as from 1 to 15 wt %, such as from 3 to 10 wt %) of propylene and from 99.9 to 75 wt % of one or more of C₂ or C₄ to C₂₀ olefin comonomer (such as ethylene or C₄ to C₁₂ alpha-olefin, such as butene, hexene, octene, decene, dodecene, such as ethylene, butene, hexene, octene).

In at least one embodiment, a polyolefin, such as a polypropylene (e.g., iPP) or an ethylene-octene copolymer, has an Mw from 40,000 to 1,500,000 g/mol, such as from 70,000 to 1,000,000 g/mol, such as from 90,000 to 500,000 g/mol, such as from 90,000 to 250,000 g/mol, such as from 90,000 to 200,000 g/mol, such as from 90,000 to 110,000 g/mol.

In at least one embodiment, a polyolefin, such as a polypropylene (e.g., iPP) or an ethylene-octene copolymer, has an Mn from 5,000 to 1,000,000 g/mol, such as from 20,000 to 160,000 g/mol, such as from 30,000 to 70,000 g/mol, such as from 40,000 to 70,000 g/mol. In at least one embodiment, a polyolefin, such as a polypropylene (e.g., iPP) or an ethylene-octene copolymer, has an Mw/Mn value from 1 to 10, such as from 1.5 to 9, such as from 2 to 7, such as from 2 to 4, such as from 2.5 to 3, for example about 2.

In at least one embodiment, a polyolefin, such as a polypropylene (e.g., iPP) or an ethylene-octene copolymer, has a melt temperature (Tm) of from 100° C. to 150° C., such as 110° C. to 140° C., such as 120° C. to 135° C., such as 130° C. to 135° C.

In at least one embodiment, a polymer of the present disclosure has a g′_(vis) of greater than 0.9, such as greater than 0.92, such as greater than 0.95.

In at least one embodiment, the polymer is an ethylene copolymer, and the comonomer is octene, at a comonomer content of from 1 wt % to 18 wt % octene, such as from 5 wt % to 15 wt %, such as from 8 wt % to 13 wt %, such as from 9 wt % to 12 wt %.

In at least one embodiment, the polymer produced has a unimodal or multimodal molecular weight distribution as determined by Gel Permeation Chromatography (GPC). By “unimodal” is meant that the GPC trace has one peak or inflection point. By “multimodal” is meant that the GPC trace has at least two peaks or inflection points. An inflection point is that point where the second derivative of the curve changes in sign (e.g., from negative to positive or vice versus).

In at least one embodiment, the polymer produced has a composition distribution breadth index (CDBI) of 50% or more, such as 60% or more, such as 70% or more. CDBI is a measure of the composition distribution of monomer within the polymer chains and is measured by the procedure described in PCT publication WO1993/003093, published Feb. 18, 1993, specifically columns 7 and 8 as well as in Wild, L. et al. (1982) “Determination of Branching Distributions in Polyethylene and Ethylene Copolymers,” J. Poly. Sci., Poly. Phys. Ed., v.20(3), pp. 441-455; and U.S. Pat. No. 5,008,204, including that fractions having a weight average molecular weight (Mw) below 15,000 are ignored when determining CDBI.

Molecular Weight, Comonomer Composition and Long Chain Branching Determination by Polymer Char GPC-IR Hyphenated with Multiple Detectors (GPC-4D)

In the event of conflict between this GPC-4D procedure and the Rapid GPC procedure below, this GPC-4D procedure shall be used.

The distribution and the moments of molecular weight (Mw, Mn, Mw/Mn, etc.), the comonomer content (C₂, C₃, C₆, etc.) and the branching index (g′) are determined by using a high temperature Gel Permeation Chromatography (Polymer Char GPC-IR) equipped with a multiple-channel band-filter based Infrared detector IRS, an 18-angle light scattering detector and a viscometer. Three Agilent PLgel 10 μm Mixed-B LS columns are used to provide polymer separation. Aldrich reagent grade 1,2,4-trichlorobenzene (TCB) with 300 ppm antioxidant butylated hydroxytoluene (BHT) is used as the mobile phase. The TCB mixture is filtered through a 0.1 μm Teflon filter and degassed with an online degasser before entering the GPC instrument. The nominal flow rate is 1 mL/min and the nominal injection volume is 200 μL. The whole system including transfer lines, columns, detectors are contained in an oven maintained at 145° C. Given amount of polymer sample is weighed and sealed in a standard vial with 80 μL flow marker (Heptane) added to it. After loading the vial in the autosampler, polymer is automatically dissolved in the instrument with 8 mL added TCB solvent. The polymer is dissolved at 160° C. with continuous shaking for about 1 hour for most PE samples or 2 hour for PP samples. The TCB densities used in concentration calculation are 1.463 g/ml at room temperature and 1.284 g/ml at 145° C. The sample solution concentration is from 0.2 to 2 mg/ml, with lower concentrations being used for higher molecular weight samples.

The concentration (c), at each point in the chromatogram is calculated from the baseline-subtracted IRS broadband signal intensity (I), using the following equation: c=βI where β is the mass constant determined with PE or PP standards. The mass recovery is calculated from the ratio of the integrated area of the concentration chromatography over elution volume and the injection mass which is equal to the pre-determined concentration multiplied by injection loop volume.

The conventional molecular weight (IR MW) is determined by combining universal calibration relationship with the column calibration which is performed with a series of monodispersed polystyrene (PS) standards ranging from 700 to 10M. The MW at each elution volume is calculated with following equation;

${\log M} = {\frac{\log\left( {K_{PS}/K} \right)}{a + 1} + {\frac{a_{PS} + 1}{a + 1}\log M_{PS}}}$ where the variables with subscript “PS” stands for polystyrene while those without a subscript are for the test samples. In this method, a_(PS)=0.67 and K_(PS)=0.00017: while a and K are calculated as described in the published in literature (Sun, T. et al. (2001) “Effect of Short Chain Branching on the Coil Dimensions of Polyolefins in Dilute Solutions,” Macromolecules, v.34(19), pp. 6812-6820), except that for purposes of this disclosure, α=0.695 and K=0.000579 for linear ethylene polymers, α=0.705 and K=0.0002288 for linear propylene polymers, α=0.695+(0.01*(wt. fraction propylene)) and K=0.000579-(0.0003502*(wt. fraction propylene)) for ethylene-propylene copolymers. Concentrations are expressed in g/cm³, molecular weight is expressed in g/mole, and intrinsic viscosity (hence K in the Mark-Houwink equation) is expressed in dL/g unless otherwise noted.

The comonomer composition is determined by the ratio of the IRS detector intensity corresponding to CH₂ and CH₃ channel calibrated with a series of PE and PP homo/copolymer standards whose nominal value are predetermined by NMR or FTIR such as EMCC commercial grades about LLDPE, Vistamaxx, ICP, etc.

The LS detector is the 18-angle Wyatt Technology High Temperature DAWN HELEOSII. The LS molecular weight (M) at each point in the chromatogram is determined by analyzing the LS output using the Zimm model for static light scattering (M. B. Huglin, Light Scattering from Polymer Solutions, Academic Press, 1971):

$\frac{K_{o}c}{\Delta{R(\theta)}} = {\frac{1}{{MP}(\theta)} + {2A_{2}c}}$ Here, ΔR(θ) is the measured excess Rayleigh scattering intensity at scattering angle θ, c is the polymer concentration determined from the IRS analysis, A₂ is the second virial coefficient. P(θ) is the form factor for a monodisperse random coil, and K_(o) is the optical constant for the system:

$K_{o} = \frac{4\pi^{2}{n^{2}\left( {{dn}/{dc}} \right)}^{2}}{\lambda^{4}N_{A}}$ where N_(A) is Avogadro's number, and (dn/dc) is the refractive index increment for the system. The refractive index, n=1.500 for TCB at 145° C. and λ=665 nm.

A high temperature Agilent (or Viscotek Corporation) viscometer, which has four capillaries arranged in a Wheatstone bridge configuration with two pressure transducers, is used to determine specific viscosity. One transducer measures the total pressure drop across the detector, and the other, positioned between the two sides of the bridge, measures a differential pressure. The specific viscosity, η_(s), for the solution flowing through the viscometer is calculated from their outputs. The intrinsic viscosity, [η], at each point in the chromatogram is calculated from the following equation: [η]=η_(s) /c where c is concentration and was determined from the IRS broadband channel output. The viscosity MW at each point is calculated from the below equation: M=K_(PS)M^(α) ^(PS) ⁺¹/[η].

The branching index (g′_(vis)) is calculated using the output of the GPC-IRS-LS-VIS method as follows. The average intrinsic viscosity, [η]_(avg), of the sample is calculated by:

$\lbrack\eta\rbrack_{avg} = \frac{\sum{c_{i}\lbrack\eta\rbrack}_{i}}{\sum c_{i}}$ where the summations are over the chromatographic slices, i, between the integration limits. The branching index g′_(vis) is defined as:

$g_{vis}^{\prime} = \frac{\lbrack\eta\rbrack_{avg}}{{kM}_{v}^{\alpha}}$ M_(v) is the viscosity-average molecular weight based on molecular weights determined by LS analysis. The K/a are for the reference linear polymers are as described above.

All the concentration is expressed in g/cm³, molecular weight is expressed in g/mole, and intrinsic viscosity is expressed in dL/g unless otherwise noted.

All molecular weights are reported in g/mol unless otherwise noted.

Differential Scanning calorimetry (DSC-Procedure-2). Melting Temperature, Tm, is measured by differential scanning calorimetry (“DSC”) using a DSCQ200 unit. The sample is first equilibrated at 25° C. and subsequently heated to 220° C. using a heating rate of 10° C./min (first heat). The sample is held at 220° C. for 3 minutes. The sample is subsequently cooled down to −100° C. with a constant cooling rate of 10° C./min (first cool). The sample is equilibrated at −100° C. before being heated to 220° C. at a constant heating rate of 10° C./min (second heat). The exothermic peak of crystallization (first cool) is analyzed using the TA Universal Analysis software and the corresponding to 10° C./min cooling rate is determined. The endothermic peak of melting (second heat) is also analyzed using the TA Universal Analysis software and the peak melting temperature (Tm) corresponding to 10° C./min. heating rate is determined. In the event of conflict between the DSC Procedure-1 and DSC procedure-2, DSC procedure-2 is used.

Blends

In another embodiment, the polymer (such as the polyethylene or polypropylene) produced is combined with one or more additional polymers prior to being formed into a film, molded part or other article. Other useful polymers include polyethylene, isotactic polypropylene, highly isotactic polypropylene, syndiotactic polypropylene, random copolymer of propylene and ethylene, and/or butene, and/or hexene, polybutene, ethylene vinyl acetate, low density polyethylene (LDPE), linear low density polyethylene (LLDPE), high density polyethylene (HDPE), ethylene vinyl acetate, ethylene methyl acrylate, copolymers of acrylic acid, polymethylmethacrylate or other polymers polymerizable by a high-pressure free radical process, polyvinylchloride, polybutene-1, isotactic polybutene, ABS resins, ethylene-propylene rubber (EPR), vulcanized EPR, EPDM, block copolymer, styrenic block copolymers, polyamides, polycarbonates, PET resins, cross linked polyethylene, copolymers of ethylene and vinyl alcohol (EVOH), polymers of aromatic monomers such as polystyrene, poly-1 esters, polyacetal, polyvinylidine fluoride, polyethylene glycols, and/or polyisobutylene.

In at least one embodiment, the polymer (such as polyethylene or polypropylene) is present in the above blends, at from 10 to 99 wt %, based upon the weight of the polymers in the blend, such as 20 to 95 wt %, such as at least 30 to 90 wt %, such as at least 40 to 90 wt %, such as at least 50 to 90 wt %, such as at least 60 to 90 wt %, such as at least 70 to 90 wt %.

The blends described above may be produced by mixing the polymers of the present disclosure with one or more polymers (as described above), by connecting reactors together in series to make reactor blends or by using more than one catalyst in the same reactor to produce multiple species of polymer. The polymers can be mixed together prior to being put into the extruder or may be mixed in an extruder.

The blends may be formed using any suitable equipment and methods, such as by dry blending the individual components and subsequently melt mixing in a mixer, or by mixing the components together directly in a mixer, such as, for example, a Banbury mixer, a Haake mixer, a Brabender internal mixer, or a single or twin-screw extruder, which may include a compounding extruder and a side-arm extruder used directly downstream of a polymerization process, which may include blending powders or pellets of the resins at the hopper of the film extruder. Additionally, additives may be included in the blend, in one or more components of the blend, and/or in a product formed from the blend, such as a film. Such additives may include, for example: fillers; antioxidants (e.g., hindered phenolics such as IRGANOX™ 1010 or IRGANOX™ 1076 available from Ciba-Geigy); phosphites (e.g., IRGAFOS™ 168 available from Ciba-Geigy); anti-cling additives; tackifiers, such as polybutenes, terpene resins, aliphatic and aromatic hydrocarbon resins, alkali metal and glycerol stearates, and hydrogenated rosins; UV stabilizers; heat stabilizers; anti-blocking agents; release agents; anti-static agents; pigments; colorants; dyes; waxes; silica; fillers; and talc.

Films

One or more of the foregoing polymers, such as the foregoing polyethylenes, polypropylenes, or blends thereof, may be used in a variety of end-use applications. Such applications include, for example, mono- or multi-layer blown, extruded, and/or shrink films. These films may be formed by extrusion or coextrusion techniques, such as a blown bubble film processing technique, where the composition can be extruded in a molten state through an annular die and then expanded to form a uni-axial or biaxial orientation melt prior to being cooled to form a tubular, blown film, which can then be axially slit and unfolded to form a flat film. Films may be subsequently unoriented, uniaxially oriented, or biaxially oriented to the same or different extents. One or more of the layers of the film may be oriented in the transverse and/or longitudinal directions to the same or different extents. The uniaxially orientation can be accomplished using typical cold drawing or hot drawing methods. Biaxial orientation can be accomplished using tenter frame equipment or a double bubble processes and may occur before or after the individual layers are brought together. For example, a polyethylene layer can be extrusion coated or laminated onto an oriented polypropylene layer or the polyethylene and polypropylene can be coextruded together into a film then oriented. Likewise, oriented polypropylene could be laminated to oriented polyethylene or oriented polyethylene could be coated onto polypropylene then optionally the combination could be oriented even further. Typically the films are oriented in the Machine Direction (MD) at a ratio of up to 15, such as from 5 to 7, and in the Transverse Direction (TD) at a ratio of up to 15, such as from 7 to 9. However, in at least one embodiment the film is oriented to the same extent in both the MD and TD directions.

The films may vary in thickness depending on the intended application; however, films of a thickness from 1 μm to 50 μm are usually suitable. Films intended for packaging are usually from 10 μm to 50 μm thick. The thickness of the sealing layer is typically 0.2 μm to 50 μm. There may be a sealing layer on both the inner and outer surfaces of the film or the sealing layer may be present on only the inner or the outer surface.

In at least one embodiment, one or more layers may be modified by corona treatment, electron beam irradiation, gamma irradiation, flame treatment, or microwave. In at least one embodiment, one or both of the surface layers is modified by corona treatment.

This disclosure further relates to:

A1. A compound represented by Formula (I): [Ar(E¹R¹R²H)_(x)(E²R³R⁴)_(y)][QR⁵R⁶R⁷R⁸]_(z)  (I) where:

each of E¹ and E² are nitrogen;

Ar is a C₁₀-C₃₀ multicyclic aromatic hydrocarbyl group, where E¹ is a first Ar substitution located on a first ring of the multicyclic aromatic hydrocarbyl group and E² is a second Ar substitution located on a second ring of the multicyclic aromatic hydrocarbyl group;

x is 1 to 4;

y is 0 to 3;

z=x;

x+y is 2 to 6;

each of R¹, R², R³, and R⁴ is independently selected from the group consisting of C₁-C₄₀ aliphatic hydrocarbyl, substituted C₁-C₄₀ aliphatic hydrocarbyl, wherein R¹, R², R³, and R⁴ together include 15 or more carbon atoms;

Q is an element selected from group 13 of the Periodic Table of the Elements; and

each of R⁵, R⁶, R⁷, and R⁸ is independently selected from the group consisting of a hydride, bridged or unbridged dialkylamido, halide, alkoxide, aryloxide, hydrocarbyl, substituted hydrocarbyl, halocarbyl, and substituted halocarbyl.

A2. The compound of A1, wherein x is 1 and y is 1.

A3. The compound of A1, wherein x is 2 and y is 0.

A4. The compound of any of A1 to A3, wherein Ar is a C₁₀-C₁₄ aromatic hydrocarbyl.

A5. The compound of any of A1 to A4, wherein Ar is naphthalene.

A6. The compound of any of A1 to A5, wherein R¹ and R³ are independently an optionally substituted C₁-C₁₀ aliphatic hydrocarbyl, and R² and R⁴ are independently an optionally substituted C₁₀-C₂₀ aliphatic hydrocarbyl.

A7. The compound of any of A1 to A6, wherein:

R¹ and R³ are methyl, and

R² and R⁴ are independently an optionally substituted C₁₀-C₂₀ aliphatic hydrocarbyl.

A8. The compound of any of A1 to A7, wherein:

R¹ and R³ are methyl, and

R² and R⁴ are independently an optionally substituted C₁₀-C₂₀ linear alkyl group.

A9. The compound of any of A1 to A8, wherein:

R¹ and R³ are methyl, and

R² and R⁴ are independently an optionally substituted C₁₈ linear aliphatic hydrocarbyl.

A10. The compound of any of A1 to A9, wherein R¹, R², R³, and R⁴ together include 24 or more carbon atoms.

A11. The compound of any of A1 to A10, wherein Q is boron.

A12. The compound of any of A1 to A11, wherein each of R⁵, R⁶, R⁷, and R⁸ is independently a C₆-C₂₄ aromatic hydrocarbyl or a substituted C₆-C₂₄ aromatic hydrocarbyl.

A13. The compound of any of A1 to A12, wherein each of R⁵, R⁶, R⁷, and R⁸ is independently a pentafluorophenyl and/or a heptafluoronaphthalenyl.

A14. The compound of A1, wherein the compound of Formula (I) is selected from the group consisting of:

1

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64

A15. The compound of A1, wherein [Ar(E¹R¹R²H)_(x)(E²R³R⁴)_(y)][QR⁵R⁶R⁷R⁸]_(z) of Formula (I) is selected from the group consisting of:

1

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A16. The compound of any of A1 to A15, wherein the compound has a solubility of more than 10 mM at 25° C. (stirred 2 hours) in methylcyclohexane. A17. The compound of any of A1 to A16, wherein the compound has a solubility of more than 1 mM at 25° C. (stirred 2 hours) in isohexane. A18. The compound of any of A1 to A17, wherein the compound has a solubility of more than 10 mM at 25° C. (stirred 2 hours) in methylcyclohexane and a solubility of more than 1 mM at 25° C. (stirred 2 hours) in isohexane. A19. A compound represented by Formula (I): [Ar(E¹R¹R²H)_(x)(E²R³R⁴)_(y)][QR⁵R⁶R⁷R⁸]_(z)  (I) wherein:

Q is an element selected from group 13 of the Periodic Table of the Elements; each of R⁵, R⁶, R⁷, and R⁸ is independently a hydride, bridged or unbridged dialkylamido, halide, alkoxide, aryloxide, hydrocarbyl, substituted hydrocarbyl, halocarbyl, or substituted halocarbyl; and the [Ar(E¹R¹R²H)_(x)(E²R³R⁴)_(y)] is selected from the group consisting of:

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A20. The compound of A19, wherein the [Ar(E¹R¹R²H)_(x)(E²R³R⁴)_(y)] is selected from the group consisting of:

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8

B1. A catalyst system comprising a catalyst and the compound of any of A1 to A20. B2. The catalyst system of B1, wherein the catalyst is represented by Formula (VI) or Formula (VII):

wherein in each of Formula (VI) and Formula (VII):

M is the metal center, and is a Group 4 metal;

n is 0 or 1;

q is 1 or 2;

T is an optional bridging group selected from dialkylsilyl, diarylsilyl, dialkylmethyl, ethylenyl or hydrocarbylethylenyl wherein one, two, three or four of the hydrogen atoms in ethylenyl are substituted by hydrocarbyl;

L₁ and L₂ are independently cyclopentadienyl, indenyl, tetrahydroindenyl or fluorenyl, optionally substituted, that are each bonded to M, or L₁ and L₂ are independently cyclopentadienyl, indenyl, tetrahydroindenyl or fluorenyl, which are optionally substituted, which two adjacent substituents on L₁ and L₂ are optionally joined to form a substituted or unsubstituted, saturated, partially unsaturated, or aromatic cyclic or polycyclic substituent;

Z is nitrogen or phosphorus;

R′ is a cyclic, linear or branched C₁ to C₄₀ alkyl or substituted alkyl group;

X₁ and X₂ are, independently, hydrogen, halogen, hydride radicals, hydrocarbyl radicals, substituted hydrocarbyl radicals, halocarbyl radicals, substituted halocarbyl radicals, silylcarbyl radicals, substituted silylcarbyl radicals, germylcarbyl radicals, or substituted germylcarbyl radicals; or both X₁ and X₂ are joined and bound to the metal atom to form a metallacycle ring containing from about 3 to about 20 carbon atoms; or both together can be an olefin, diolefin or aryne ligand.

B3. The catalyst system of any of B1 to B2, wherein the catalyst is C₂ symmetrical.

B4. The catalyst system of B1, wherein the catalyst is rac-dimethylsilyl-bis(indenyl)hafnium dimethyl or and 1,1′-bis(4-triethylsilylphenyl)methylene-(cyclopentadienyl)(3,8-di-tertiary-butyl-1-fluorenyl)hafnium dimethyl.

B5. The catalyst system of B1, wherein the catalyst is one or more of:

-   bis(1-methyl, 3-n-butyl cyclopentadienyl) M(R)₂; -   dimethylsilyl bis(indenyl)M(R)₂; -   bis(indenyl)M(R)₂; -   dimethylsilyl bis(tetrahydroindenyl)M(R)₂; -   bis(n-propylcyclopentadienyl)M(R)₂; -   dimethylsilyl (tetramethylcyclopentadienyl)(cyclododecylamido)M(R)₂; -   dimethylsilyl (tetramethylcyclopentadienyl)(cyclododecylamido)M(R)₂; -   dimethylsilyl (tetramethylcyclopentadienyl)(t-butylamido)M(R)₂; -   dimethylsilyl (tetramethylcyclopentadienyl)(t-butylamido)M(R)₂; -   μ-(CH₃)₂Si(cyclopentadienyl)(1-adamantylamido)M(R)₂; -   μ-(CH₃)₂Si(3-tertbutylcyclopentadienyl)(1-adamantylamido)M(R)₂; -   μ-(CH₃)₂(tetramethylcyclopentadienyl)(1-adamantylamido)M(R)₂; -   μ-(CH₃)₂Si(tetramethylcyclopentadienyl)(1-adamantylamido)M(R)₂; -   μ-(CH₃)₂C(tetramethylcyclopentadienyl)(1-adamantylamido)M(R)₂; -   μ-(CH₃)₂Si(tetramethylcyclopentadienyl)(1-tertbutylamido)M(R)₂; -   μ-(CH₃)₂Si(fluorenyl)(1-tertbutylamido)M(R)₂; -   μ-(CH₃)₂Si(tetramethylcyclopentadienyl)(1-cyclododecylamido)M(R)₂; -   μ-(C₆H₅)₂C(tetramethylcyclopentadienyl)(1-cyclododecylamido)M(R)₂; -   μ-(CH₃)₂Si(η⁵-2,6,6-trimethyl-1,5,6,7-tetrahydro-s-indacen-1-yl)(tertbutylamido)M(R)₂;     where M is selected from Ti, Zr, and Hf; and R is selected from     halogen or C₁ to C₅ alkyl.     C1. A method of polymerizing olefins to produce polyolefin     comprising contacting one or more olefins with the catalyst system     of any of B1 to B5, and obtaining a polyolefin.     C2. The method of Cl, wherein the olefins comprise ethylene and/or     propylene.     C3. The method of any of C1 to C2, wherein the method is performed     in the solution phase.     D1. A catalyst system comprising a catalyst compound and the     compound of any of A1 to A20, wherein the catalyst compound is     represented by Formula (VIII), Formula (IX), or Formula (X):

wherein:

M is a group 3, 4, 5, 6, 7, 8, 9, 10, 11, or 12 metal;

J is group including a three-atom-length bridge between the quinoline and the amido nitrogen;

E is carbon, silicon, or germanium;

X is an anionic leaving group;

L is a neutral Lewis base;

R¹ and R¹³ are independently selected from the group including of hydrocarbyls, substituted hydrocarbyls, and silyl groups;

R², R³, R⁴, R⁵, R⁶, R⁷, R⁸, R⁹, R¹⁰, R^(10′), R¹¹, R^(11′), R¹², and R¹⁴ are independently hydrogen, hydrocarbyl, alkoxy, silyl, amino, aryloxy, substituted hydrocarbyl, halogen, or phosphino;

n is 1 or 2;

m is 0, 1, or 2, where n+m is not greater than 4; and

two R groups are optionally joined to form a substituted hydrocarbyl, unsubstituted hydrocarbyl, substituted heterocyclic, or unsubstituted heterocyclic, saturated or unsaturated ring, where the ring has 5, 6, 7, or 8 ring atoms and where substitutions on the ring can join to form additional rings;

two X groups are optionally joined together to form a dianionic group;

two L groups are optionally joined together to form a bidentate Lewis base; and

X group is optionally joined to an L group to form a monoanionic bidentate group.

D2. A catalyst system comprising a catalyst compound and the compound of any of A1 to A20, wherein the catalyst compound is represented by the Formula (XI):

wherein M is a Group 4 metal; X¹ and X² are independently a univalent C₁-C₂₀ hydrocarbyl, C₁-C₂₀ substituted hydrocarbyl, a heteroatom or a heteroatom-containing group, or X¹ and X² join together to form a C₄-C₆₂ cyclic or polycyclic ring structure; each R¹, R², R³, R⁴, R⁵, R⁶, R⁷, R⁸, R⁹, and R¹⁰ is independently hydrogen, C₁-C₄₀ hydrocarbyl, C₁-C₄₀ substituted hydrocarbyl, a heteroatom or a heteroatom-containing group, or two or more of R¹, R², R³, R⁴, R⁵, R⁶, R⁷, R⁸, R⁹, or R¹⁰ are optionally joined together to form a C₄-C₆₂ cyclic or polycyclic ring structure, or a combination thereof; Q is a neutral donor group; J is heterocycle, a substituted or unsubstituted C₇-C₆₀ fused polycyclic group, where at least one ring is aromatic and where at least one ring, which may or may not be aromatic, has at least five ring atoms' G is as defined for J or may be hydrogen, C₂-C₆₀ hydrocarbyl, C₁-C₆₀ substituted hydrocarbyl, or optionally independently form a C₄-C₆₀ cyclic or polycyclic ring structure with R⁶, R⁷, or R⁸ or a combination thereof; Y is divalent C₁-C₂₀ hydrocarbyl or divalent C₁-C₂₀ substituted hydrocarbyl or (-Q-Y—) together form a heterocycle; and heterocycle may be aromatic and/or may have multiple fused rings. D3. A catalyst system comprising a catalyst compound and the compound of any of A1 to A20, wherein the catalyst compound is represented by the Formula (XIV):

wherein:

A is chlorine, bromine, iodine, —CF₃ or —OR¹¹;

each of R¹ and R² is independently hydrogen, C₁-C₂₂-alkyl, C₂-C₂₂-alkenyl, C₆-C₂₂-aryl, arylalkyl where alkyl has from 1 to 10 carbon atoms and aryl has from 6 to 20 carbon atoms, or five-, six- or seven-membered heterocyclyl comprising at least one atom selected from the group consisting of N, P, O and S;

wherein each of R¹ and R² is optionally substituted by halogen, —NR¹¹ ₂, —OR¹¹ or —SiR¹² ₃;

wherein R¹ optionally bonds with R³, and R² optionally bonds with R⁵, in each case to independently form a five-, six- or seven-membered ring;

R⁷ is a C₁-C₂₀ alkyl;

each of R³, R⁴, R⁵, R⁸, R⁹, R¹⁰, R¹⁵, R¹⁶, and R¹⁷ is independently hydrogen, C₁-C₂₂-alkyl, C₂-C₂₂-alkenyl, C₆-C₂₂-aryl, arylalkyl where alkyl has from 1 to 10 carbon atoms and aryl has from 6 to 20 carbon atoms, —NR¹¹ ₂, —OR¹¹, halogen, —SiR¹² ₃ or five-, six- or seven-membered heterocyclyl comprising at least one atom selected from the group consisting of N, P, O, and S;

wherein R³, R⁴, R⁵, R⁷, R⁸, R⁹, R¹⁰, R¹⁵, R¹⁶, and R¹⁷ are optionally substituted by halogen, —NR¹¹ ₂, —OR¹¹ or —SiR¹² ₃;

wherein R³ optionally bonds with R⁴, R⁴ optionally bonds with R⁵, R⁷ optionally bonds with R¹⁰, R¹⁰ optionally bonds with R⁹, R⁹ optionally bonds with R⁸, R¹⁷ optionally bonds with R¹⁶, and R¹⁶ optionally bonds with R¹⁵, in each case to independently form a five-, six- or seven-membered carbocyclic or heterocyclic ring, the heterocyclic ring comprising at least one atom from the group consisting of N, P, O and S;

R¹³ is C₁-C₂₀-alkyl bonded with the aryl ring via a primary or secondary carbon atom;

R¹⁴ is chlorine, bromine, iodine, —CF₃ or —OR¹¹, or C₁-C₂₀-alkyl bonded with the aryl ring;

each R¹¹ is independently hydrogen, C₁-C₂₂-alkyl, C₂-C₂₂-alkenyl, C₆-C₂₂-aryl, arylalkyl where alkyl has from 1 to 10 carbon atoms and aryl has from 6 to 20 carbon atoms, or —SiR¹² ₃, wherein R¹¹ is optionally substituted by halogen, or two R¹¹ radicals optionally bond to form a five- or six-membered ring;

each R¹² is independently hydrogen, C₁-C₂₂-alkyl, C₂-C₂₂-alkenyl, C₆-C₂₂-aryl, arylalkyl where alkyl has from 1 to 10 carbon atoms and aryl has from 6 to 20 carbon atoms, or two R² radicals optionally bond to form a five- or six-membered ring;

each of E¹, E², and E³ is independently carbon, nitrogen or phosphorus;

each u is independently 0 if E¹, E², and E³ is nitrogen or phosphorus and is 1 if E¹, E², and E³ is carbon;

each X is independently fluorine, chlorine, bromine, iodine, hydrogen, C₁-C₂₀-alkyl, C₂-C₁₀-alkenyl, C₆-C₂₀-aryl, arylalkyl where alkyl has from 1 to 10 carbon atoms and aryl has from 6 to 20 carbon atoms, —NR¹⁸ ₂, —OR¹⁸, —SO₃R¹⁸, —OC(O)R¹⁸, —CN, —SCN, β-diketonate, —CO, —BF₄ ⁻, —PF₆ ⁻ or bulky non-coordinating anions, and the radicals X can be bonded with one another;

each R¹⁸ is independently hydrogen, C₁-C₂₀-alkyl, C₂-C₂₀-alkenyl, C₆-C₂₀-aryl, arylalkyl where alkyl has from 1 to 10 carbon atoms and aryl has from 6 to 20 carbon atoms, or —SiR¹⁹ ₃, wherein R¹⁸ can be substituted by halogen or nitrogen- or oxygen-containing groups and two R¹⁸ radicals optionally bond to form a five- or six-membered ring;

each R¹⁹ is independently hydrogen, C₁-C₂₀-alkyl, C₂-C₂₀-alkenyl, C₆-C₂₀-aryl or arylalkyl where alkyl has from 1 to 10 carbon atoms and aryl has from 6 to 20 carbon atoms, wherein R¹⁹ can be substituted by halogen or nitrogen- or oxygen-containing groups or two R¹⁹ radicals optionally bond to form a five- or six-membered ring;

s is 1, 2, or 3;

D is a neutral donor; and

t is 0 to 2.

D4. A catalyst system comprising a catalyst compound and the compound of any of A1 to A20, wherein the catalyst compound is represented by the Formula (XV):

wherein M represents a transition metal atom selected from the groups 3 to 11 metals in the periodic table; k is an integer of 1 to 6; m is an integer of 1 to 6; R^(a) to R^(f) may be the same or different from one another and each represent a hydrogen atom, a halogen atom, a hydrocarbon group, a heterocyclic compound residue, an oxygen-containing group, a nitrogen-containing group, a boron-containing group, a sulfur-containing group, a phosphorus-containing group, a silicon-containing group, a germanium-containing group or a tin-containing group, among which 2 or more groups are optionally bound to each other to form a ring; when k is 2 or more, R^(a) groups, R^(b) groups, R^(c) groups, R^(d) groups, R^(e) groups, or R^(f) groups may be the same or different from one another, one group of R^(a) to R^(f) contained in one ligand and one group of R^(a) to R^(f) contained in another ligand may form a linking group or a single bond, and a heteroatom contained in R^(a) to R^(f) may coordinate with or bind to M; m is a number satisfying the valence of M; Y represents a hydrogen atom, a halogen atom, an oxygen atom, a hydrocarbon group, an oxygen-containing group, a sulfur-containing group, a nitrogen-containing group, a boron-containing group, an aluminum-containing group, a phosphorus-containing group, a halogen-containing group, a heterocyclic compound residue, a silicon-containing group, a germanium-containing group or a tin-containing group; when m is 2 or more, a plurality of groups represented by Q may be the same or different from one another, and a plurality of groups represented by Q may be mutually bound to form a ring.

D5. A catalyst system comprising a catalyst compound and the compound of any of A1 to A20, wherein the catalyst compound is represented by the Formula (XVI):

wherein:

M is Co or Fe; each X is an anion; n is 1, 2 or 3, so that the total number of negative charges on said anion or anions is equal to the oxidation state of a Fe or Co atom present in Formula (XVI);

R¹, R² and R³ are each independently hydrogen, hydrocarbyl, substituted hydrocarbyl, or an inert functional group;

R⁴ and R⁵ are each independently hydrogen, hydrocarbyl, an inert functional group or substituted hydrocarbyl;

R⁶ is represented by the Formula (XVII):

and R⁷ is Formula (XVIII):

wherein R⁸ and R¹³ are each independently hydrocarbyl, substituted hydrocarbyl or an inert functional group;

R⁹, R¹⁰, R¹¹, R¹⁴, R¹⁵ and R¹⁶ are each independently hydrogen, hydrocarbyl, substituted hydrocarbyl or an inert functional group;

R¹² and R¹⁷ are each independently hydrogen, hydrocarbyl, substituted hydrocarbyl or an inert functional group;

and provided that two of R⁸, R⁹, R¹⁰, R¹¹, R¹², R¹³, R¹⁴, R¹⁵, R¹⁶ and R¹⁷ that are adjacent to one another, together optionally form a ring.

D6. A catalyst system comprising a catalyst compound and the compound of any of A1 to A20, wherein the catalyst compound is represented by the Formula (XIX):

M¹ is selected from the group consisting of titanium, zirconium, hafnium, vanadium, niobium, tantalum, chromium, molybdenum and tungsten; each of Q¹, Q², Q³, and Q⁴ is independently oxygen or sulfur; R¹ and R² are independently hydrogen, halogen, hydroxyl, hydrocarbyl, or substituted hydrocarbyl, optionally R¹ and R² may also be joined together to form an alkanediyl group or a conjugated C₄-C₄₀ diene ligand which is coordinated to M¹;

each of R⁴, R⁵, R⁶, R⁷, R⁸, R⁹, R¹⁰, R¹¹, R¹², R¹³, R¹⁴, R¹⁵, R¹⁶, R¹⁷, R¹⁸, and R¹⁹ is independently hydrogen, halogen, C₁-C₄₀ hydrocarbyl or C₁-C₄₀ substituted hydrocarbyl, —NR′₂, —SR′, —OR, —OSiR′₃, —PR′₂, where each R is hydrogen, halogen, C₁-C₁₀ alkyl, or C₆-C₁₀ aryl, or one or more of R⁴ and R⁵, R⁵ and R⁶, R⁶ and R⁷, R⁸ and R⁹, R⁹ and R¹⁰, R¹⁰ and R¹¹, R¹² and R¹³, R¹³ and R¹⁴, R¹⁴ and R¹⁵, R¹⁶ and R¹⁷, R¹⁷ and R¹⁸, and R¹⁸ and R¹⁹ are optionally joined to form a saturated ring, unsaturated ring, substituted saturated ring, or substituted unsaturated ring;

R³ is a C₁-C₄₀ unsaturated alkyl or substituted C₁-C₄₀ unsaturated alkyl.

D7. A catalyst system comprising a catalyst compound and the compound of any of A1 to A20, wherein the catalyst compound is represented by the Formula (XX) or (XXI):

wherein M is a Group 3 to 12 transition metal or a Group 13 or 14 main group metal; each X is independently a leaving group; y is 0 or 1 (when y is 0 group L′ is absent); ‘n’ is the oxidation state of M and is +3, +4, or +5; ‘m’ represents the formal charge of the YZL or the YZL′ ligand, and is 0, −1, −2 or −3; L is a Group 15 or 16 element; L′ is a Group 15 or 16 element or Group 14 containing group; Y is a Group 15 element; Z is a Group 15 element; R¹ and R² are, independently, a C₁ to C₂₀ hydrocarbon group, a heteroatom containing group having up to twenty carbon atoms, silicon, germanium, tin, lead, or phosphorus; R³ is optionally absent or may be a hydrocarbon group, a hydrogen, a halogen, a heteroatom containing group; R⁴ and R⁵ are independently an alkyl group, an aryl group, substituted aryl group, a cyclic alkyl group, a substituted cyclic alkyl group, a cyclic aralkyl group, a substituted cyclic aralkyl group, or multiple ring system; R⁶ and R⁷ are independently absent, hydrogen, an alkyl group, halogen, heteroatom, or a hydrocarbyl group; R* may be absent, or may be a hydrogen, a Group 14 atom containing group, a halogen, or a heteroatom containing group. E1. A method of polymerizing olefins to produce a polyolefin, the method comprising contacting at least one olefin with the catalyst system of D1, and obtaining a polyolefin. E2. A method of polymerizing olefins to produce a polyolefin, the method comprising contacting at least one olefin with the catalyst system of D2, and obtaining a polyolefin. E3. A method of polymerizing olefins to produce a polyolefin, the method comprising contacting at least one olefin with the catalyst system of D3, and obtaining a polyolefin. E4. A method of polymerizing olefins to produce a polyolefin, the method comprising contacting at least one olefin with the catalyst system of D4, and obtaining a polyolefin. E5. A method of polymerizing olefins to produce a polyolefin, the method comprising contacting at least one olefin with the catalyst system of D5, and obtaining a polyolefin. E6. A method of polymerizing olefins to produce a polyolefin, the method comprising contacting at least one olefin with the catalyst system of D6, and obtaining a polyolefin. E7. A method of polymerizing olefins to produce a polyolefin, the method comprising contacting at least one olefin with the catalyst system of D7, and obtaining a polyolefin. F1. A solution comprising the compound of any of A1 to A20 and an aliphatic solvent wherein the solution is substantially free of aromatic solvents. F2. A solution comprising the catalyst system of any of claims B1-B5 or D1-D7 and an aliphatic solvent wherein the solution is substantially free of aromatic solvents. G1. A composition comprising the catalyst system of any of B1-B5 or D1-D7 and an aliphatic solvent wherein the solution is substantially free of aromatic solvents.

Experimental

Lithium tetrakis(pentafluorophenyl)borate etherate (Li-BF20) was purchased from Boulder Scientific. N,N-Dimethylanilinium tetrakis(pentafluorophenyl)borate (DMAH-BF20) was purchased from Albemarle Corporation, Baton Rouge, La. Sodium tetrakis(heptafluoronaphthalen-2-yl)borate (Na-BF28) and N,N-dimethylanilinium tetrakis(heptafluoronaphthalen-2-yl)borate (DMAH-BF28) were purchased from Grace Davison.

¹H NMR for Compound Characterization: Chemical structures are determined by ¹H NMR. ¹H NMR data are collected at room temperature (e.g., 23° C.) in a 5 mm probe. The ¹H NMR measurements were recorded on a 400 MHz or 500 MHz Bruker spectrometer with chemical shifts referenced to residual solvent peaks (CDCl₃: 7.27 ppm for ¹H, 77.23 ppm for ¹³C).

All anhydrous solvents were purchased from Sigma-Aldrich. Deuterated solvents were purchased from Cambridge Isotope Laboratories.

EXAMPLES

Borate anions and ammonium cations used as activator components are shown in Scheme 1.

Synthesis of Activators

General Synthesis of Ammonium Borate Activators: Ammonium borate activators were prepared using a two-step process. In the first step, an amine was dissolved in a solvent (e.g. hexane, cyclohexane, methylcyclohexane, ether, dichloromethane, toluene) and an excess (ca. 1.2 molar equivalents) of hydrogen chloride was added to form an ammonium chloride salt. The salt was isolated by filtration from the reaction medium and dried under reduced pressure. The isolated ammonium chloride was then heated to reflux with one molar equivalent of an alkali metal borate in a solvent (e.g. cyclohexane, dichloromethane, methylcyclohexane) to form the ammonium borate along with byproduct alkali metal chloride, the latter which typically is removed by filtration. Examples describing the synthetic details for selected ammonium borates are given below.

N¹,N⁵-dimethylnaphthalene-1,5-diamine: Formic acid (38.1 mL, 1 mol) and acetic acid (77.6 mL, 821 mol) were combined and heated at 60° C. for 3 hours. After cooling to 0° C., a 200 mL THF solution of naphthalene-1,5-diamine (25 g, 158 mmol) was added slowly and the reaction stirred at ambient temperature overnight. A lavender precipitate formed which was collected, washed with hexane, and dried under a stream of nitrogen. The powdery solid was obtained in 78% yield and used subsequently. Lithium aluminum hydride (16.7 g, 420 mmol) was suspended in 500 mL of THF and the formamide (15 g, 70 mmol) was added slowly. After stirring at ambient temperature overnight, the reaction was slowly quenched with ice. Ether was added and the mixture filtered through a plug of silica gel to give a purple solid in 72% yield: ¹H NMR (500 MHz, CDCl₃, δ): 2.49 (s, 6H), 3.87 (br s, 2H), 6.51 (m, 2H), 7.01 (m, 2H), 7.34 (m, 2H).

N¹,N⁵-dimethyl-N¹,N⁵-dioctadecylnaphthalene-1,5-diamine: The above naphthalenediamine (2.5 g, 13.4 mmol) and bromooctadecane (9.4 g, 28.2 mmol) were dissolved in 200 mL of THF. Sodium hydride (95%, 0.71 g, 28.2 mmol) was added slowly and the reaction heated at 70° C. for over 24 hours. The reaction was cooled to room temperature, diluted with diethyl ether, and quenched with ice water. The organic portion was washed with brine, dried, filtered and concentrated. The crude solid was recrystallized with hot isohexane to give the alkylated product as a white solid: ¹H NMR (500 MHz, C₆D₆, δ): 0.90 (m, 6H), 1.35 (m, 60H), 1.59 (m, 4H), 2.71 (s, 6H), 3.00 (m, 4H), 7.06 (d, J=7.0 Hz, 2H), 7.43 (m, 2H), 8.35 (d, J=8.5 Hz, 2H); ¹³C NMR: 14.0 (2C), 22.8 (2C), 27.3-29.8 (28C), 29.8 (2C), 32.0 (2C), 42.5 (2C), 27.1 (2C), 115.8 (2C), 119.5 (2C), 125.0 (2C), 131.8 (2C), 151.1 (2C).

N-methyl-5-(methyhoctadecyl)amino)-N-octadecylnaphthalen-1-aminium chloride: To the above alkylated naphthalenediamine (3.0 g, 4.77 mmol) dissolved in 50 mL of hexane was added HCl (2.8 mL, 2M in ether). A white precipitate formed after approximately 10 minutes and the reaction stirred at ambient temperature overnight.

N-methyl-5-(methyhoctadecyl)amino)-N-octadecylnaphthalen-1-aminium tetrakis(pentafluorophenyl)borate: The above HCl salt (0.500 g, 0.687 mmol) was slurried with Li—CF20 (0.522 g, 0.687 mmol) in isohexane and heated at 55° C. for 1.5 hours. The reaction mixture was allowed to cool to ambient and stir overnight. The solvent was removed and the residue redissolved in methylene chloride, then filtered through Celite. Concentration of the filtrate gave the product as a brown solid in 48% yield.

N-methyl-5-(methyhoctadecyl)amino)-N-octadecylnaphthalen-1-aminium tetrakis(heptafluoronaphthalen-2-yl)borate: The HCl salt (0.500 g, 0.687 mmol) described above was suspended in 20 mL of isohexane and combined with Na-BF28 (0.719 g, 0.687 mmol). The mixture was heated at 55° C. for 1.5 hours, then cooled to ambient and filtered. The solid was dissolved in methylene chloride, filtered through Celite, and then concentrated to give a brown solid in 83% yield.

Polymerization in Parallel Pressure Reactor

Solvents, polymerization-grade toluene, and isohexane were supplied by ExxonMobil Chemical Company and purified by passing through a series of columns: two 500 cc Oxyclear cylinders in series from Labclear (Oakland, Calif.), followed by two 500 cc columns in series packed with dried 3 Å mole sieves (8-12 mesh; Aldrich Chemical Company), and two 500 cc columns in series packed with dried 5 Å mole sieves (8-12 mesh; Aldrich Chemical Company). 1-octene (C₈) and 1-hexene (C₆) (98%, Aldrich Chemical Company) were dried by stirring over NaK overnight followed by filtration through basic alumina (Aldrich Chemical Company, Brockman Basic 1).

Polymerization-grade ethylene (C₂) was used and further purified by passing the gas through a series of columns: 500 cc Oxyclear cylinder from Labclear (Oakland, Calif.) followed by a 500 cc column packed with dried 3 Å mole sieves (8-12 mesh; Aldrich Chemical Company) and a 500 cc column packed with dried SA mole sieves (8-12 mesh; Aldrich Chemical Company).

Polymerization grade propylene (C₃) was used and further purified by passing the propylene through a series of columns: 2,250 cc Oxiclear cylinder from Labclear followed by a 2,250 cc column packed with 3 Å mole sieves (8-12 mesh; Aldrich Chemical Company), then two 500 cc columns in series packed with 5 Å mole sieves (8-12 mesh; Aldrich Chemical Company), then a 500 cc column packed with Selexsorb CD (BASF), and finally a 500 cc column packed with Selexsorb COS (BASF).

Unless stated otherwise, solutions of the metal complexes and activators were prepared in a drybox using toluene or methylcyclohexane. Concentrations were typically 0.2 mmol/L. Tri-n-octylaluminum (TNOAL, neat, AkzoNobel) was typically used as a scavenger. Concentration of the TNOAL solution in toluene was from 0.5 to 2 mmol/L.

Polymerizations were carried out in a parallel pressure reactor, as generally described in U.S. Pat. Nos. 6,306,658; 6,455,316; 6,489,168; WO 2000/009255; and Murphy, V. et al. (2003) “A Fully Integrated High-Throughput Screening Methodology for the Discovery of New Polyolefin Catalysts: Discovery of a New Class of High Temperature Single-Site Group (IV) Copolymerization Catalysts,” J. Am. Chem. Soc., v.125, pp. 4306-4317, each of which is incorporated by reference. The experiments were conducted in an inert atmosphere (N₂) drybox using autoclaves equipped with an external heater for temperature control, glass inserts (internal volume of reactor=23.5 mL for C₂ and C₂/C₈; 22.5 mL for C₃ runs), septum inlets, regulated supply of nitrogen, ethylene and propylene, and equipped with disposable PEEK mechanical stirrers (800 RPM). The autoclaves were prepared by purging with dry nitrogen at 110° C. or 115° C. for 5 hours and then at 25° C. for 5 hours. Although the specific quantities, temperatures, solvents, reactants, reactant ratios, pressures, and other variables are frequently changed from one polymerization run to the next, the following describes a typical polymerization performed in a parallel pressure reactor.

RUN A: Ethylene-octene copolymerization (EO). A series of ethylene-octene polymerizations were performed in the parallel pressure reactor according to the procedure described above. In these studies rac-dimethylsilyl-bis(indenyl)hafnium dimethyl (MCN-1) was used along with ammonium borate activators. In a typical experiment an automated syringe was used to introduce into the reactor the following reagents, if utilized, in the following order: isohexane (0.50 mL), 1-octene (100 μL), additional isohexane (0.50 mL), an isohexane solution of TNOAL scavenger (0.005 M, 100 μL), additional isohexane (0.50 mL), a toluene solution of the respective polymerization catalyst (110 μL, 0.2 mM), additional isohexane (0.50 mL), a toluene solution of the respective activator (110 μL, 0.2 mM), then additional isohexane so that the total solvent volume for each run was 5 mL. Catalyst and activator were used in a 1:1.1 ratio. Each reaction was performed at a specified temperature from 50° C. to 120° C., typically 100° C., while applying about 100 psig of ethylene (monomer) gas. Each reaction was allowed to run for about 20 minutes (˜1,200 seconds) or until approximately 20 psig of ethylene gas uptake was observed, at which point the reactions were quenched with air (˜300 psig). When sufficient polymer yield was attained (e.g., at least ˜10 mg), the polyethylene product was analyzed by Rapid GPC, described below. Run conditions and data are reported in Table 1.

TABLE 1 Data for the ethylene-octene copolymerization. activity octene yield (kg/ incorporation T_(m) Activator time (s) (g) mmol/h) M_(w) M_(n) PDI (wt %) (° C.) 1 DMAH- 20.2 0.075 668 213,996 109,520 2.0 — 45.9 BF20 2 DMAH- 18.3 0.070 689 203,689 118,987 1.7 31.9 45.0 BF20 3 DMAH- 22.6 0.066 526 255,979 146,513 1.7 22.0 64.1 BF20 4 DMAH- 25.6 0.051 359 292,671 148,073 2.0 25.7 73.0 BF20 5 DMAH- 27.2 0.069 457 380,061 213,127 1.8 — 51.6 BF28 6 DMAH- 27.9 0.065 419 384,224 222,601 1.7 28.2 56.1 BF28 7 DMAH- 27.7 0.064 416 418,110 223,004 1.9 — 64.9 BF28 8 DMAH- 29.4 0.059 361 456,087 246,798 1.8 21.6 73.2 BF28 9 DANH- 23.1 0.070 545 236,059 127,504 1.9 20.1 48.4 BF20 10 DANH- 18.8 0.069 661 246,786 123,369 2.0 28.4 53.3 BF20 11 DANH- 24.1 0.060 448 253,394 137,531 1.8 — 67.1 BF20 12 DANH- 21.6 0.059 492 271,642 140,636 1.9 23.6 71.6 BF20 13 DANH- 27.4 0.071 466 370,694 191,509 1.9 — 48.8 BF28 14 DANH- 26.7 0.066 445 398,148 220,874 1.8 28.7 50.1 BF28 15 DANH- 26.1 0.061 421 401,600 225,714 1.8 — 66.9 BF28 16 DANH- 28.6 0.063 397 461,954 261,335 1.8 26.9 77.6 BF28 General conditions: catalyst = 20 nmol; activator = 22 nmol; 1-octene = 100 μL; solvent = isohexane; volume = 5 mL; tri(n-octyl)aluminum = 500 nmol; T = 100° C.; P = 100 PSI

RUN B: Ethylene homopolymerization (PE). A series of ethylene polymerizations were performed in the parallel pressure reactor according to the procedure described above. In these studies rac-dimethylsilyl-bis(indenyl)hafnium dimethyl (MCN-1) was used along with ammonium borate activators. In a typical experiment an automated syringe was used to introduce into the reactor the following reagents, if utilized, in the following order: isohexane (0.50 mL), an isohexane solution of TNOAL scavenger (0.005 M, 60 μL), additional isohexane (0.50 mL), a toluene solution of the respective polymerization catalyst (110 μL, 0.2 mM), additional isohexane (0.50 mL), a toluene solution of the respective activator (110 μL, 0.2 mM), then additional isohexane so that the total solvent volume for each run was 5 mL. Catalyst and activator were used in a 1:1.1 ratio. Each reaction was performed at a specified temperature from 50° C. to 120° C., typically 100° C., while applying about 100 psig of ethylene (monomer) gas. Each reaction was allowed to run for about 20 minutes (˜1,200 seconds) or until approximately 20 psig of ethylene gas uptake was observed, at which point the reactions were quenched with air (˜300 psig). When sufficient polymer yield was attained (e.g., at least ˜10 mg), the polyethylene product was analyzed by Rapid GPC, described below. Run conditions and data are reported in Table 2.

TABLE 2 Data for the ethylene homopolymerization activity yield (kg/ T_(m) Entry Activator time (s) (g) mmol/h) M_(w) M_(n) PDI (° C.) 1 DMAH-BF20 24.6 0.052 380 532,719 259,194 2.1 134.7 2 DMAH-BF20 19.9 0.057 516 465,599 217,830 2.1 134.7 3 DMAH-BF20 20.2 0.051 454 496,760 224,010 2.2 134.4 4 DMAH-BF20 23.1 0.047 366 483,392 235,608 2.1 134.8 5 DMAH-BF28 46.6 0.065 251 691,837 362,479 1.9 134.5 6 DMAH-BF28 25.4 0.061 432 644,765 313,730 2.1 134.7 7 DMAH-BF28 22.4 0.055 442 511,907 248,632 2.1 134.9 8 DMAH-BF28 22.5 0.052 416 579,071 300,489 1.9 135.1 9 DANH-BF20 25.3 0.057 406 575,637 266,923 2.2 134.9 10 DANH-BF20 25.9 0.059 410 557,398 241,622 2.3 134.9 11 DANH-BF20 23.2 0.057 442 558,409 252,760 2.2 134.4 12 DANH-BF20 21.4 0.054 454 494,008 223,513 2.2 134.9 13 DANH-BF28 28.3 0.061 388 606,748 268,585 2.3 134.7 14 DANH-BF28 30.7 0.062 364 704,918 324,671 2.2 134.9 15 DANH-BF28 22.2 0.059 478 627,550 299,681 2.1 134.6 16 DANH-BF28 23.8 0.055 416 626,411 285,161 2.2 134.7 General conditions: catalyst = 20 nmol; activator = 22 nmol; 1-octene = 100 μL; solvent = isohexane; volume = 5 mL; tri(n-octyl)aluminum = 500 nmol; T = 100° C.; P = 100 PSI

RUN C: Propylene homopolymerization (PP). The parallel pressure reactor was prepared as described above and purged with propylene. In these polymerizations, the metallocene rac-dimethylsilyl-bis(indenyl)hafnium dimethyl (MCN-1) was used along with several different ammonium borate activators. The activators were prepared in solutions of toluene. Isohexane was then injected into each vessel at room temperature followed by a predetermined amount of propylene gas. The reactor was heated to the set temperature while stirring at 800 rpm, and the scavenger, activator and catalyst solutions were injected sequentially to each vessel. The polymerization was allowed to proceed as described previously. Each reaction was allowed to run for about 20 minutes (˜1,200 seconds) or until approximately 4 psig of propylene gas uptake was observed. Run conditions and data are reported in Table 2.

TABLE 3 Data for the propylene homopolymerization activity time (kg/ # Activator (s) yield (g) mmol/h) Mw Mn PDI T_(m) (° C.) 1 DMAH-BF20 63.9 0.074 208 46,838 26,867 1.7 120 2 DMAH-BF20 84.4 0.083 177 53,488 33,956 1.6 115 3 DMAH-BF20 85.9 0.076 159 48,339 29,541 1.6 114 4 DMAH-BF20 114.5 0.069 108 58,165 36,066 1.6 122 5 DMAH-BF20 92.5 0.065 126 55,911 33,355 1.7 121 6 DMAH-BF20 102.3 0.056 99 51,967 26,257 2.0 121 7 DMAH-BF28 72.6 0.070 174 104,441 65,509 1.6 125 8 DMAH-BF28 100.7 0.068 122 117,743 73,932 1.6 126 9 DMAH-BF28 180.6 0.072 72 111,191 69,544 1.6 126 10 DMAH-BF28 133.7 0.065 88 114,496 65,644 1.7 126 11 DMAH-BF28 155.1 0.065 75 153,830 96,426 1.6 129 12 DMAH-BF28 458.3 0.052 20 124,708 74,048 1.7 126 13 DMAH-BF28 144.6 0.066 82 141,317 79,382 1.8 126 14 DMAH-BF28 107.7 0.061 102 127,730 78,854 1.6 127 15 DANH-BF20 1201.0 0.038 6 51,438 33,922 1.5 117 16 DANH-BF20 468.1 0.046 18 56,174 32,576 1.7 117 17 DANH-BF20 202.1 0.047 42 49,592 28,864 1.7 115 18 DANH-BF20 229.5 0.051 40 58,465 36,929 1.6 117 19 DANH-BF20 194.5 0.051 47 51,619 31,664 1.6 120 20 DANH-BF20 146.7 0.048 59 55,353 33,105 1.7 121 22 DANH-BF20 1201.6 0.031 5 64,550 38,775 1.7 117 23 DANH-BF28 127.8 0.066 93 101,895 64,934 1.6 125 24 DANH-BF28 117.0 0.066 102 107,664 66,209 1.6 127 25 DANH-BF28 141.8 0.064 81 122,386 78,916 1.6 127 26 DANH-BF28 108.7 0.068 113 113,090 65,431 1.7 126 27 DANH-BF28 133.9 0.066 89 114,992 77,613 1.5 125 28 DANH-BF28 129.5 0.056 78 122,126 77,826 1.6 126 29 DANH-BF28 219.5 0.050 41 124,717 81,609 1.5 126 30 DANH-BF28 152.8 0.053 62 110,456 71,967 1.5 125 General conditions: catalyst = 20 nmol; activator = 22 nmol; solvent = isohexane; volume = 5 mL; tri(n-octyl)aluminum = 500 nmol; T = 100° C.; P = 160 PSI

FIGS. 1-3 show catalyst system activity of the catalyst systems described above when used with comparative example activators (COMP EX1 and COMP EX2) and example activators (EX 1 and EX2). COMP EX 1 is a catalyst system including MCN-1 catalyst, and DMAH-BF20. COMP EX 2 is a catalyst system including MCN-1 catalyst, and DMAH-BF28. EX 1 is a catalyst system including MCN-1 catalyst, and DANH-BF20. EX 2 is a catalyst system including MCN-1 catalyst, and DANH-BF28.

FIG. 1 is a graph depicting ethylene polymerization activity with catalyst systems, COMP EX1, EX1, COMP EX2, and EX2, showing comparable activities, without the need for aromatic hydrocarbon solubilization of the activators.

FIG. 2 is a graph depicting propylene polymerization activity with catalyst systems COMP EX1, EX1, COMP EX2, and EX2, showing comparable activities, without the need for aromatic hydrocarbon solubilization of the activators.

FIG. 3 is a graph depicting ethylene:octene polymerization activity with catalyst systems COMP EX1, EX1, COMP EX2, and EX2, showing comparable activities, without the need for aromatic hydrocarbon solubilization of the activators.

High Throughput Polymer Characterization. Polymer sample solutions were prepared by dissolving polymer in 1,2,4-trichlorobenzene (TCB, 99+% purity from Sigma-Aldrich) containing 2,6-di-tert-butyl-4-methylphenol (BHT, 99% from Aldrich) at 165° C. in a shaker oven for approximately 3 hours. The typical concentration of polymer in solution was from 0.1 to 0.9 mg/mL with a BHT concentration of 1.25 mg BHT/mL of TCB.

Rapid GPC

To determine various molecular weight related values by GPC, high temperature size exclusion chromatography was performed using an automated “Rapid GPC” system as generally described in U.S. Pat. Nos. 6,491,816; 6,491,823; 6,475,391; 6,461,515; 6,436,292; 6,406,632; 6,175,409; 6,454,947; 6,260,407; and 6,294,388; each of which is fully incorporated by reference. The apparatus has a series of three 30 cm×7.5 mm linear columns, each containing PLgel 10 μm, Mix B. The GPC system was calibrated using polystyrene standards ranging from 580 to 3,390,000 g/mol. The system was operated at an eluent flow rate of 2 mL/minutes and an oven temperature of 165° C. 1,2,4-trichlorobenzene was used as the eluent. The polymer samples were dissolved in 1,2,4-trichlorobenzene at a concentration of 0.28 mg/mL and 400 uL of a polymer solution was injected into the system. The concentration of the polymer in the eluent was monitored using an evaporative light scattering detector. The molecular weights presented are relative to linear polystyrene standards and are uncorrected, unless indicated otherwise.

Differential Scanning calorimetry

(DSC-Procedure 1) measurements were performed on a TA-Q100 instrument to determine the melting point (T_(m)) of the polymers. Samples were pre-annealed at 220° C. for 15 minutes and then allowed to cool to room temperature overnight. The samples were then heated to 220° C. at a rate of 100° C./min and then cooled at a rate of 50° C./min Melting points were collected during the heating period.

The weight percent of ethylene incorporated in polymers was determined by rapid FT-IR spectroscopy on a Bruker Equinox 55+IR in reflection mode. Samples were prepared in a thin film format by evaporative deposition techniques. FT-IR methods were calibrated using a set of samples with a known wt % ethylene content. For ethylene-1-octene copolymers, the wt % octene in the copolymer was determined via measurement of the methyl deformation band at ˜1,375 cm⁻¹. The peak height of the deformation band at ˜1,375 cm⁻¹ was normalized by the combination and overtone band at ˜4,321 cm⁻¹, which corrects for path length differences.

Overall, it has been discovered that NCA activators including a diamino multicyclic aromatic ring structure may be used in olefin polymerization reactions. Additionally, the use of such activators provides catalyst systems with higher polymerization activity than previous catalyst systems. Furthermore, the activators are soluble in aliphatic hydrocarbon solvents and polymers may be produced with reduced or eliminated aromatic hydrocarbon content. The polymers produced may have higher Mw and/or higher melt temperature compared to polymers produced with previous catalyst systems.

The phrases, unless otherwise specified, “consists essentially of” and “consisting essentially of” do not exclude the presence of other steps, elements, or materials, whether or not, specifically mentioned in this specification, so long as such steps, elements, or materials, do not affect the basic and novel characteristics of this disclosure, additionally, they do not exclude impurities and variances normally associated with the elements and materials used.

For the sake of brevity, only certain ranges are explicitly disclosed herein. However, ranges from any lower limit may be combined with any upper limit to recite a range not explicitly recited, as well as, ranges from any lower limit may be combined with any other lower limit to recite a range not explicitly recited, in the same way, ranges from any upper limit may be combined with any other upper limit to recite a range not explicitly recited. Additionally, a range includes every point or individual value between its end points even though not explicitly recited. Thus, every point or individual value may serve as its own lower or upper limit combined with any other point or individual value or any other lower or upper limit, to recite a range not explicitly recited.

All documents described herein are incorporated by reference herein, including any priority documents and/or testing procedures to the extent they are not inconsistent with this text. As is apparent from the foregoing general description and the specific embodiments, while forms of this disclosure have been illustrated and described, various modifications can be made without departing from the spirit and scope of this disclosure. Accordingly, it is not intended that this disclosure be limited thereby. Likewise whenever a composition, an element or a group of elements is preceded with the transitional phrase “including,” it is understood that we also contemplate the same composition or group of elements with transitional phrases “consisting essentially of,” “consisting of,” “selected from the group of consisting of,” or “is” preceding the recitation of the composition, element, or elements and vice versa. The compounds, catalyst systems, and processes disclosed may be practiced in the absence of any element which is not disclosed herein.

While the present disclosure has been described with respect to a number of embodiments and examples, those skilled in the art, having benefit of this disclosure, will appreciate that other embodiments can be devised which do not depart from the scope and spirit of the present disclosure. 

What is claimed is:
 1. A compound represented by Formula (I): [Ar(E¹R¹R²H)_(x)(E²R³R⁴)_(y)]^(x+)([QR⁵R⁶R⁷R⁸]⁻)_(z)  (I) where: each of E¹ and E² are nitrogen; Ar is a C₁₀-C₃₀ multicyclic aromatic hydrocarbyl group, where E¹ is a first Ar substitution located on a first ring of the multicyclic aromatic hydrocarbyl group and E² is a second Ar substitution located on a second ring of the multi-cyclic aromatic hydrocarbyl group; x is 1 to 4; y is 0 to 3; z=x; x+y is 2 to 6; each of R¹, R², R³, and R⁴ is independently selected from the group consisting of C₁-C₄₀ aliphatic hydrocarbyl, substituted C₁-C₄₀ aliphatic hydrocarbyl, wherein R¹, R², R³, and R⁴ together include 15 or more carbon atoms; Q is an element selected from group 13 of the Periodic Table of the Elements; and each of R⁵, R⁶, R⁷, and R⁸ is independently selected from the group consisting of a hydride, bridged or unbridged dialkylamido, halide, alkoxide, aryloxide, hydrocarbyl, substituted hydrocarbyl, halocarbyl, and substituted halocarbyl.
 2. The compound of claim 1, wherein x is 1 and y is
 1. 3. The compound of claim 1, wherein x is 2 and y is
 0. 4. The compound of claim 1, wherein Ar is a C₁₀-C₁₄ aromatic hydrocarbyl.
 5. The compound of claim 4, wherein Ar is naphthalene.
 6. The compound of claim 1, wherein R¹ and R³ are independently an optionally substituted C₁-C₁₀ aliphatic hydrocarbyl, and R² and R⁴ are independently an optionally substituted C₁₀-C₂₀ aliphatic hydrocarbyl.
 7. The compound of claim 6, wherein: R¹ and R³ are methyl, and R² and R⁴ are independently an optionally substituted C₁₀-C₂₀ aliphatic hydrocarbyl.
 8. The compound of claim 6, wherein: R¹ and R³ are methyl, and R² and R⁴ are independently an optionally substituted C₁₀-C₂₀ linear alkyl group.
 9. The compound of claim 6, wherein: R¹ and R³ are methyl, and R² and R⁴ are independently an optionally substituted C₁₈ linear aliphatic hydrocarbyl.
 10. The compound of claim 1, wherein R¹, R², R³, and R⁴ together include 24 or more carbon atoms.
 11. The compound of claim 1, wherein Q is boron.
 12. The compound of claim 1, wherein each of R⁵, R⁶, R⁷, and R⁸ is independently a C₆-C₂₄ aromatic hydrocarbyl or a substituted C₆-C₂₄ aromatic hydrocarbyl.
 13. The compound of claim 12, wherein each of R⁵, R⁶, R⁷, and R⁸ is independently a pentafluorophenyl and or a heptafluoronaphthalenyl.
 14. The compound of claim 1, wherein the compound of Formula (I) is selected from the group consisting of: 1

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15. The compound of claim 1, wherein [Ar(E¹R¹R²H)_(x)(E²R³R⁴)_(y)]^(x+) of Formula (I) is selected from the group consisting of: 1

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16. The compound of claim 1, wherein the compound has a solubility of more than 10 mM at 25° C. (stirred 2 hours) in methylcyclohexane and a solubility of more than 1 mM at 25° C. (stirred 2 hours) in isohexane.
 17. A compound represented by Formula (I): [Ar(E¹R¹R²H)_(x)(E²R³R⁴)_(y)]^(x+)([QR⁵R⁶R⁷R⁸]⁻)_(z)  (I) wherein: Q is an element selected from group 13 of the Periodic Table of the Elements; each of R⁵, R⁶, R⁷, and R⁸ is independently a hydride, bridged or unbridged dialkylamido, halide, alkoxide, aryloxide, hydrocarbyl, substituted hydrocarbyl, halocarbyl, or substituted halocarbyl; and the [Ar(E¹R¹R²H)_(x)(E²R³R⁴)_(y)]^(x+) is selected from the group consisting of: 1

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18. The compound of claim 17, wherein the [Ar(E¹R¹R²H)_(x)(E²R³R⁴)_(y)] is selected from the group consisting of: 1

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19. A catalyst system comprising a catalyst and the compound of claim
 1. 20. The catalyst system of claim 19, wherein the catalyst is represented by Formula (VI) or Formula (VII):

wherein in each of Formula (VI) and Formula (VII): M is the metal center, and is a Group 4 metal; n is 0 or 1; q is 1 or 2; T is an optional bridging group selected from dialkylsilyl, diarylsilyl, dialkylmethyl, ethylenyl or hydrocarbylethylenyl wherein one, two, three or four of the hydrogen atoms in ethylenyl are substituted by hydrocarbyl; L₁ and L₂ are independently cyclopentadienyl, indenyl, tetrahydroindenyl or fluorenyl, optionally substituted, that are each bonded to M, or L₁ and L₂ are independently, cyclopentadienyl, indenyl, tetrahydroindenyl or fluorenyl, which are optionally substituted, in which two adjacent substituents on L₁ and L₂ are optionally joined to form a substituted or unsubstituted, saturated, partially unsaturated, or aromatic cyclic or polycyclic substituent; Z is nitrogen or phosphorus; R′ is a cyclic, linear or branched C₁ to C₄₀ alkyl or substituted alkyl group; X₁ and X₂ are, independently, hydrogen, halogen, hydride radicals, hydrocarbyl radicals, substituted hydrocarbyl radicals, halocarbyl radicals, substituted halocarbyl radicals, silylcarbyl radicals, substituted silylcarbyl radicals, germylcarbyl radicals, or substituted germylcarbyl radicals; or both X₁ and X₇ are joined and bound to the metal atom to form a metallacycle ring containing from about 3 to about 20 carbon atoms; or both together can be an olefin, diolefin or aryne ligand. 